Colorant liquid, method of use, and wildland fire retardant liquids containing same

Abstract

An aqueous dispersion of a fugitive-color colorant is added to an ante-colorized fire retardant composition to form a colorized fire retardant composition.

Description

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention is directed to aqueous fire retardant compositions containing an emulsified or suspended colorant. In particular, the present invention is directed to aqueous fire retardant compositions containing emulsified or suspended colorants produced by the emulsion or suspension polymerization of a monomer or a mixture of monomers in the presence of at least one dye.

The present invention is also directed to processes of preparing the fire retardant compositions, containing an emulsified or suspended colorant, wherein the colorants are produced by emulsion or suspension polymerization of a mixture of at least one monomer and at least one dye.

2. Related Background Art

A variety of fire retardant solutions are known. “Evaluation of Megatard 2700: A Proposed New Fire Retardant System”, C. W. George and C. W. Johnson, U.S.D.A. Forest Service, Intermountain Forest and Range Experimental Station, General Technical Report INT-112, August 1981, describes a fire retardant system containing ammonium sulfate as the active fire retardant salt, a guar gum thickener, iron oxide as a colorant, a spoilage inhibitor, and corrosion inhibitors. In this case, the fire retardant composition is prepared by mixing the ammonium sulfate and the corrosion inhibitor to form a liquid component. The iron oxide, thickener, and spoilage inhibitor are mixed with water to form a slurry. The slurry and the liquid component are then mixed in equal volumes to form the mixed fire retardant which is then loaded onto an airplane and applied to a wildland fire. E. P. A. Artsybashev, V. G. Lorberbaum, T. G. Pirogova, and M. A. Potemin, 12 Lesnoe Khozyaistvo 43, 44 (1991) describes a fire retardant consisting of 30-37% diammonium phosphate, 16-20% urea, 8-10% ammonium chloride, 16-20% sodium carboxymethyl cellulose, 3-5% acid orange dye, and 7-20% kaolin. E. S. Artsybashev, V. G. Loberbaum, I. N. Sedina, T. G. Pirogova, and E. F. Davydov, 6 Lesnoe Khozyaistvo 40, 42 (1988) describes a fire retardant consisting of 62-75t diammonium phosphate, 23-35% urea, 2-3% sulphonol, and 0.5% acid dye applied as a 13% aqueous solution.

Phosphate solutions useful for fire-retardant compositions are described in U.S. Pat. Nos. 3,223,649, 3,257,316, 3,275,566, 3,293,189, 3,338,829, 3,342,749, 3,350,305, 3,364,149, and 3,634,234. Other fire-retardant compositions containing various ammonium salts are described in U.S. Pat. Nos. 3,309,324, 4,101,485, 4,145,296, and 4,272,414. Fire retardant compositions stabilized with galactomannan gum are described in U.S. Pat. Nos. 4,447,336, 4,447,337, and 4,606,831. V. G. Lorberbaum, I. N. Sedina, E. E. Frolovskii, V. I. Fedorov and E. F. Davydov, 9 Lesnoe Khozyaistvo 59, 60 (1983) describes a fire retardant containing 90.2% hydrated magnesium chloride, 8.2-5.82% wetting agent, 1.25-0.89% corrosion inhibitor, and 1.25-0.89t light-resistant acid orange dye in powder form which is dissolved in water prior to application. E. A. Shchetinskii, A. M. Simskii, and E. F. Davydov, 5 Lesnoe Khozyaistvo 88 (1975) describes a fire retardant containing Rhodamine-S dye added to aqueous solutions of diammonium phosphate, ammonium sulfate, or “ammophos”. Chemical Week, Mar. 28, 1979, at page 40, describes a fire retardant, PHOS-CHEK® XAF made by Monsanto Company (St. Louis, Mo.) which contains the active ingredient diammonium phosphate and a fugitive International Orange color that fades away after several days, as opposed to the permanent red iron oxide pigment previously used.

French Patent Publication No. FR 2172867 A describes fire extinguishing solutions that contain mono or diammonium phosphate, a solid surfactant, and a colorant. Russian Patent Publication No. RU 2022630 describes a unit for the preparation of fire extinguishing compounds. The unit contains a motor pump connected to an ejection mixer with the powder supplied from a bunker, and a static mixer in the output line.

Soviet Patent Publication No. SU 1544451 describes compositions for fighting forest fires from the air containing sodium carboxymethyl cellulose, ammonium hydrogen phosphate, ammonium chloride, urea, kaolin, and light fast acid orange as a dye. Soviet Patent Publication No. SU 15444450 describes compositions for fighting forest fires from the ground level containing urea, sulphonol, scarlet acid dye, diammonium hydrogen phosphate, and ammonium chloride. International Patent Publication No. WO 9322000 describes compositions for the prevention and the combatting of fires containing fiber/clay combinations, corrosion inhibitors, anti-cryptogamic agents, a dye, and cellulose based fibers.

U.S. Pat. No. 4,168,239 describes thixotropic emulsion concentrates, used to form fire suppressant foams for fire fighting, that contain oil, emulsifier, colorant, and an aqueous fire suppressant. U.S. Pat. No. 3,730,890 describes flame retardant concentrates formed from attapuglite clay suspended in liquid ammonium polyphosphate. U.S. Pat. No. 3,960,735 describes flame retardant polyphosphate compositions containing iron cyanide blue added to inhibit the corrosion of aluminum. The above U.S. patents are incorporated by reference herein.

U.S. Pat. No. 3,409,550 describes fire retardant compositions containing a mixture of ammonium sulfate and diammonium phosphate in an aqueous gel. Dyes such as Rhodamine B, azo red A, naphthol orange, and pigments may be added as a marking agent. U.S. Pat. Nos. 4,839,065, 4,971,728, and 4,983,326 describe a fire retardant concentrate containing a thickening agent and a fire retardant. The diammonium phosphate, diammonium sulfate, and monoammonium phosphate blended with polyammonium phosphate are used as the fire retardant. The above U.S. patents are incorporated by reference herein.

Colorants are chemical substances added to materials to produce color effects. The colorants used in the present invention can be aqueous dispersions of a non-fluorescent pigment or of a fluorescent pigment as described in U.S. Pat. Nos. 5,294,664 and 5,215,679. The above U.S. patents are incorporated by reference herein.

Although the term “fire retardant solution” is used herein, it is understood that such fire retardant liquid mixtures are not true solutions in which all of the components are dissolved to form a single homogenous liquid phase—without solid phases or other immiscible liquid phases present. It will be recognized that some of the components used may be essentially insoluble in the liquid components. That is, components such as iron oxide and titanium oxide, as well as some of the polymeric components, are insoluble in water. Nonetheless, the term “solution” will be used as well as the more physicochemically correct terms such as “fluid” or “liquid” because the term is commonly used in this art. Thus, the term “fire retardant solution” is used to mean the fire retardant composition formed by water and other liquid and/or solid components ready for application onto burning fuels.

The terms “dispersion” and “suspension,” as will be described below, are differentiated herein from “slurry”. Accordingly, phrases such as “dispersion solution,” “aqueous dispersion,” “aqueous suspension,” “suspension solution,” “suspension,” or “dispersion” are not interchangeable with “slurry solution,” or “slurry.”

It is conventional practice to add the components of a fire retardant solution, as a preformed concentrate, into water at a prescribed mix (dilution) ratio in order to form the fire retardant solution. There are conventionally three types of fire retardant concentrates—“dry-powder” concentrates, “fluid” concentrates, and “liquid” concentrates. “Dry-powder” type concentrates are simply dry mixtures of components that are mixed into water in order to form a fire retardant solution.

Mixtures of components are formed in accordance with the teachings of U.S. Pat. Nos. 4,839,065, 4,971,728 and 4,983,326 to prepare low viscosity fire retardant concentrates which are referred to as “fluid concentrates”. The fluid concentrate type fire retardants are delivered to the mixing or dilution location or depot in the fluid concentrates' low viscosity concentrated form. When the fluid concentrates are subsequently diluted with water, at their prescribed mix ratios, suspended thickeners are activated and gum-thickened fire retardant solutions are prepared. The level of viscosity obtained upon dilution of the fluid concentrate can be altered by varying the amount of gum-thickener incorporated in the formulation.

A third type of wildland fire retardant concentrate, prepared according to the teachings of U.S. Pat. Nos. 3,730,890 and 3,960,735, is referred to as “liquid concentrates”. In this case, liquid ammonium phosphate-containing fertilizer solutions, optionally combined with color pigments, clay used as a suspension agent, corrosion inhibitors, and other functional components, form unthickened fire retardant concentrate suspensions. The liquid concentrate type fire retardants are delivered to the mixing or dilution location or depot as a high viscosity suspension. When the liquid concentrates are subsequently diluted with water, at their prescribed mix ratios, low viscosity ammonium phosphate fire retardant solutions containing, optionally, color pigment, clay and other functional components are obtained. These solutions are formed by dilution immediately prior to use in order to prevent separation and settling of the solids from the liquid.

Although both “fluid” and “liquid” type concentrates are fluid or liquid mixtures, the terms have a particular meaning in the art. The difference between the fluid concentrate and the liquid concentrate type fire retardants is apparent. A fluid concentrate exhibits a low viscosity until diluted with water. At that time, suspended thickeners are activated and the viscosity of the resultant solution remains unaffected, or increases, depending on the amount of thickener in the concentrated composition. A liquid concentrate, on the other hand, is a relatively high viscosity liquid mixture containing suspended clay, fire retardant, and colorizing pigment that, upon dilution at the prescribed mix ratio, forms an unthickened fire retardant solution.

Accordingly, the terms “liquid” and “fluid” when used in the phrases “liquid concentrate” and “fluid concentrate” have specific meaning. When the terms “liquid” and “fluid” are used elsewhere, they are intended to have their common meaning—referring to the physical phase of matter that conforms to a volume and that is substantially incompressible. Although, as described previously, the terms “liquid” and “fluid” include mixtures of liquids with undissolved solid particles.

Fire retardant solutions used to combat and control wildland fires are applied from the ground or from the air. Application from the ground is usually from a vehicle such as a fire engine, while application from the air is usually from an airplane or helicopter. It is often desirable to mark the locations that have been applied with fire retardants in order to coordinate fire-fighting activities, to conserve supplies, and to show the progress of the fire-fighting effort. Therefore, color pigments are often added to the fire-fighting product formulation at the time of the product's manufacture.

The fuel which feeds a wildland fire varies widely from grasses to large trees. Therefore, the color pigment in the applied fire retardant must present an adequate color contrast from the background fuel to conveniently show where fire retardant has been applied. The pigmented fire retardants of the prior art, however, might contain too much or too little colorant for a particular application because, while the color and geometry of wildland fuels vary widely, the concentration of pigment is fixed at the time of fire retardant manufacture at the factory.

Accordingly, it would be desirable to have the capability of adjusting the colorant level in the fire retardant solution at the time of use relative to the amount needed to maintain visibility. This ability would both minimize the possibility of leaving unobserved discontinuities in the retardant fire break through which a fire could escape, and minimize the use of colorant in those instances when visibility is easily achieved. Either case would result in savings in cost and possibly property.

Excess application of colorant further has an impact on the aesthetics of the wildland. Towards minimizing such impact, the United States Forest Service regulates that a film of a colorized formulation must return to the color of the uncolorized film after a prescribed amount of sunlight, currently 18,000 Langleys (7.53×10 8 J/M 2 ) of exposure per U.S. Department of Agriculture, Forest Service, Specification for Long Term Retardant, Forest Fire, Aircraft or Ground Application, Specification 5100-304a, February 1986. According to that specification, a 0.022 inch (0.056 cm) thick film of the fire retardant solution is applied to a glass plate. The plate is then exposed to natural light in accordance with ASTM G-24, Standard Recommended Practice for Conducting Natural Light Exposures, until 18,000 Langleys (7.53×10 8 J/M 2 ) are accumulated. The requirement is that “the mixed retardant with fugitive colorant shall not be of a color different from the mixed retardant without colorant” after exposure to 18,000 Langleys (7.53×10 8 J/M 2 ) as provided by the above protocols.

Therefore, it is desirable for fire retardant liquids to contain colorants that are visible for a limited period of time after application but then fade and become non-visible. Colorants that fade are called fugitive colorants. The color effects that fugitive colorants impart are called fugitive colors. The pigments titanium dioxide TiO 2 (not presently used commercially in wildland fire retardants) and iron oxide Fe 2 O 3 do not produce color effects that inherently fade. Thus, to the extent that titanium dioxide is opaquely white and iron oxide is strongly red, they are non-fugitive colorants. Consequently, as non-fugitive colorants, titanium dioxide and iron oxide are not suitable for use in a truly fugitive colored fire retardant solution.

SUMMARY OF THE INVENTION

The fire retardant systems of the present invention includes an ante-colorized fire retardant composition and an aqueous pigment dispersion colorant that, in combination, form a colorized fire retardant composition. The colorant system of this invention includes the aqueous pigment dispersion colorant and the dispersion's pigment formed from a polymer and a dye. The pigment has properties effective to allow the pigment to be dispersed in water to form the aqueous pigment dispersion and to cause the aqueous pigment dispersion to remain stable, resisting sedimentation without agitation, until the dispersion is used to form colorized fire retardant liquids.

The aqueous pigment dispersion colorant is added to the ante-colorized fire retardant composition, in order to form a colorized fire retardant composition, at any time prior to or during discharge of the thus formed colorized fire retardant composition. The colorized fire retardant composition is generally discharged towards the fuel, or potential fuel, of a fire that the fire retardant composition is used to try to control. Accordingly, “fuel” is that which can burn. Fuels include, for example, grass, brush, shrub, trees, timber, artificial structures and constructions, and mobile units.

As used herein, the phrase “ante-colorized fire retardant composition” is used to indicate the fire retardant composition or liquid to which is added the colorant employed by the present invention. The ante-colorized fire retardant composition or liquid can itself be already colorized. Further, the ante-colorized fire retardant composition or liquid can be a solution, a mixture, an emulsion, or a suspension.

The term “dye” as used herein means colorant compounds that are dissolved in the media in which they are used. The term “pigment” as used herein refers to colorizing compounds that are insoluble in the media in which they are used and consequently are present as solid particles.

The terms “emulsion,” “dispersion,” and “suspension” as used herein mean solid/liquid mixtures in which the solid does not readily separate out from the liquid, prior to the use of the emulsion, dispersion, or suspension, even in the absence of agitation or some other energy being imparted to the dispersion. The liquid can include dissolved solids. The term “slurry” as used herein means a solid/liquid mixture in which the solid does separate out from the liquid in the absence of agitation or some other energy being imparted to the mixture. It is understood by one of ordinary skill in the art that, other parameters being equal, slurries are formed by larger sized particles than the smaller sized particles that form emulsions, dispersions, or suspensions.

The important advantageous property of the aqueous pigment dispersions of this invention is the resistance of the aqueous pigment dispersions to settling of the solid components from the liquid components. Accordingly, it is understood that as used herein, the terms emulsion, dispersion, and suspension can be used interchangeably except where a specific process is recited that would not produce an emulsion, a dispersion, or a suspension. The use of one term, for example “dispersion,” below generally includes the other terms such as emulsion or suspension. The solid/liquid mixtures of the colorants of this invention will be generally referred to below as “aqueous pigment dispersions” while the pigment in the aqueous pigment dispersion will be generally referred to below as “aqueous dispersion pigment.”

The percentage units used herein to describe composition constituents are in percent by weight unless specifically indicated otherwise.

In one aspect, this invention utilizes a pigment containing a dye in an amount effective to impart a desired level of color intensity to the pigment. The pigment comprises a water insoluble polymer formed from at least four monomers, at least one monomer selected from each of the following groups (a) through (d):

a. from about 40% to about 78.5% total polymer weight of a water insoluble vinyl monomer free of polar groups;

b. from about 15% to about 35% by total polymer weight of vinyl nitrile;

c. from about 1.5% to about 5% by total polymer weight of a vinyl monomer containing a least one sulfonate group; and

d. from about 5% to about 20% total polymer weight of a polar vinyl monomer selected from:

(i) polar acrylate esters;

(ii) polar methacrylate esters;

(iii) vinyl acetate;

(iv) a substituted acrylamide containing hydroxyl or carboxylic ester groups; or

(v) mixtures thereof.

The aqueous pigment dispersion includes water in an amount to provide a total solids content of from about 0.5% to less than 100% by weight.

In another aspect, the present invention utilizes a colorant, which is an aqueous emulsion of a water insoluble tetra polymer which contains a fluorescent or non-fluorescent dye, comprising:

a. a water insoluble tetra polymer from about 25-50% by weight;

b. a dye from about 0.1-10% by weight;

c. an anionic emulsifier from about 0.2-10% by weight; and

d. water from about 30-74.7% by weight;

with the water insoluble tetra polymer comprising:

A) a water insoluble vinyl monomer free of polar groups from about 52-65% by weight;

B) acrylonitrile from about 25-35% by weight;

C) a vinyl monomer containing at least one sulfonate group from about 1.5-4.%% by weight; and

D) a polar vinyl monomer from about 5-15% by weight selected from:

i) polar, nonchlorinated, nonepoxidized acrylate esters;

ii) vinyl acetate; or

iii) a substituted acrylamide containing hydroxyl or carboxylic ester groups.

In yet another aspect of the present invention, a colorized fire retardant liquid utilizes a colorant, which is an aqueous emulsion of a water insoluble tetra polymer which contains a fluorescent or non-fluorescent dye, comprising:

a) a water insoluble tetra polymer from about 35-45% by weight;

b) a dye from about 0.5-7% by weight;

c) an anionic emulsifier from about 0.5-5.5% by weight; and

d) water from about 46-64% by weight;

with the water insoluble tetra polymer comprising:

A) a water insoluble vinyl monomer free of polar groups from about 52-65% by weight;

B) acrylonitrile from about 25-35% by weight;

C) a vinyl monomer containing sulfonate groups from about 1.5-4.5% by weight; and

D) a polar vinyl monomer from about 5-15% by weight selected from:

i) polar, nonchlorinated, nonepoxidized acrylate esters;

ii) vinyl acetate; or

iii) a substituted acrylamide containing OH or carboxylic ester groups.

In still another aspect, the present invention utilizes a colorant which is a fluorescent or non-fluorescent pigment comprising:

I. a tetra polymer, which is comprised of:

a) a water insoluble vinyl monomer free of polar groups from about 52-65% by weight;

b) acrylonitrile from about 25-35% by weight;

c) a vinyl monomer containing sulfonate groups from about 1.5-4.5% by weight; and

d) a polar vinyl monomer from about 5-15% by weight selected from:

1) polar, nonchlorinated, nonepoxidized acrylate esters;

2) vinyl acetate; or

3) a substituted acrylamide containing hydroxyl or carboxylic ester groups; and

II. a fluorescent or non-fluorescent dye.

DETAILED DESCRIPTION OF THE INVENTION

Aqueous pigment dispersion colorants, being already dispersed, are more easily dispersed in a fire retardant solution than are dry-powder pigment colorants. Without being bound by theory, this difference in the ease of dispersion is believed to result from the fact that the pigment particles are present in the aqueous pigment dispersions as individual, discrete and separate particles whereas the dry-powder pigments tend to exist in the dry state as agglomerates. Such agglomerates require a considerable energy input to achieve the same degree of ultimate dispersion as the pre-dispersed pigments in the aqueous pigment dispersions.

Accordingly, the colorant component of the present invention, which are aqueously emulsified or suspended pigments, can be advantageously added directly to a neat fire retardant solution, in order to form the colorized fire retardant solution of the present invention, at any time before applying the colorized fire retardant solution to a fire or to fuel threatened by a fire. It is particularly advantageous to add the aqueously emulsified or suspended colorant shortly before the thus formed colorized fire retardant solution is used, such as at the time that the delivery (or application) vehicle is being loaded with the fire retardant solution, or just before, or as the colorized fire retardant is discharged to the fuel. The emulsified or suspended colorant is of a particle size effective to maintain the dispersion of the pigment particles, with little or no agitation, prior to use of the dispersion. By contrast, agitation is required when pigment slurries are used, without which the solid particles would settle out from the liquid prior to using the slurry.

The colorized fire retardant solutions of the present invention are sufficiently-stable from settling or separation of the dispersed pigment from the liquid so that the colorized fire retardant solutions can be mixed ahead of the time of use. In particular, the viscosity stability during storage may be improved when the aqueous pigment dispersion is present. Nevertheless, it is advantageous to mix the fire retardant solution at or shortly before use in-order to be able to adapt to changing visibility, fire, and fuel conditions.

Generally, fire retardant solutions are applied to large fires from the air by means of being released from helicopters or fixed-wing aircraft. Some aircraft can drop partial loads by discharging from different compartments or by shutting off the discharge after partial release. Nevertheless, in order to maximize the payload of fire retardant solution, other cargo is minimized. Consequently, it is preferred that the mixing to form the colorized fire retardant solutions of this invention be performed just prior to or during the loading of the thus formed colorized fire retardant solution onto the aircraft.

In certain situations such as, for example, when the fire retardant solution is applied from a hose or applied in multiple metered doses, it is advantageous to add the aqueously emulsified or suspended colorant just before or as the colorized fire retardant is discharged to the fuel.

By a method of the present invention, the aqueously emulsified or suspended colorant component can be added to the fire retardant solution to form the colorized fire retardant solution as the colorized fire retardant solution is being discharged to the fuel. This method advantageously allows immediate and continuing adjustment of the color component of the colorized fire retardant solution in response to changing visibility, fire, and fuel conditions.

The present invention utilizes pigment powders that are polymeric compounds incorporating at least one dye constituent. It is preferred that the dye constituents are incorporated into the polymeric compound during the polymerization of the constituent monomers that form the polymeric compound. The polymeric compound can be formed from one or more monomer compounds of any convenient moiety or moieties. The aqueous pigment dispersion colorant of this invention is formed by dispersing the polymeric pigment powder (incorporating the dye) in water or other aqueous media effective to form an emulsion or suspension. One particular process by which the polymeric pigment powder (incorporating the dye) is dispersed in water or other aqueous media is by polymerization in situ within the aqueous medium in which the polymeric pigment powder thus formed is dispersed.

According to one embodiment of the present invention, a colorized fire retardant solution is formed from a fire retardant solution and a colorant in an amount effective to colorize the fire retardant solution, wherein the colorant is an aqueous dispersion of a fluorescent or non-fluorescent pigment, and wherein the aqueous dispersion is an emulsion or a suspension.

Another embodiment of the present invention is directed to a method for forming a colorized fire retardant solution from an ante-colorized fire retardant solution. The method comprises adding an aqueous dispersion of a fluorescent or non-fluorescent pigment to the ante-colorized fire retardant solution, in an amount effective to colorize said ante-colorized fire retardant solution, at a time proximate to discharging the colorized fire retardant solution to a fuel. The method can include monitoring a parameter and adjusting the amount of aqueous pigment dispersion in response to the monitored parameter. The amount of aqueous pigment dispersion can be added incrementally, at a rate effective to colorize the ante-colorized fire retardant solution, as the colorized fire retardant solution is loaded onto the applying vehicle or, possibly, as it is discharged from the applying vehicle onto the target fuel. The rate can be adjusted in response to the monitored parameter.

Yet another embodiment of the present invention is directed to a method to optically mark fuel comprising adding a colorant to an ante-colorized fire retardant solution, at a rate effective to colorize the ante-colorized fire retardant solution; discharging the colorized fire retardant solution to form a discharge;. directing the discharge to mark the fuel; monitoring a parameter; and adjusting the rate that the pigment is added responsively to the monitored parameter.

The parameter monitored can be any conveniently measured property such as a color of the fuel, a reflectance of the fuel, a color of the colorized fire retardant solution, the wind conditions, the ambient temperature, or the temperature or smoking character of the fire.

The present invention, as described above, utilizes pigment particles that are polymeric compounds incorporating at least a dye. The aqueous pigment dispersion colorant of this invention is formed by dispersing the polymeric pigment particles (incorporating the dye) in water effective to form an emulsion or suspension. The average particle size of the polymeric pigment particles used to form the aqueous pigment dispersion colorant of this invention should be less than 10 μm, preferably less than about 5 μm, more preferably less than about 1 μm average particle size. The smaller size particles are more effective at remaining dispersed or suspended in water, without settling, when-agitation or other energy is not imparted to the emulsion, dispersion, or suspension.

It is advantageous for the average particle size be from about 0.35 μm to about 0.55 μm. It is more advantageous for the average particle size be from about 0.35 μm to about 0.45 μm. The more consistent small size distribution causes the emulsion, dispersion, or suspension to be better emulsified, dispersed, or suspended in the water.

The pigments used in the aqueous pigment dispersion colorant of this invention can be processed by any convenient method to produce particles with sufficiently small particle sizes that will remain in an emulsion, dispersion, or suspension. For example, theoretically solid pigments can be ground to small particle sizes. However, it is only with great difficulty that grinding processes can produce average particle sizes less than about 1 μm. Accordingly, it is preferred that the polymer pigments of this invention be formed by an emulsion or suspension polymerization process. Such processes can easily form particles in situ having average particle sizes less than 1 μm, and as low as about 0.01 μm or less.

It may be desirable to include opacifying pigments such as, for example, titanium dioxide, by incorporating such pigments in the aqueous dispersion pigment. Such components can be incorporated by any convenient method such as, for example, by inclusion during the in situ polymerization of the fugitive pigments to form the aqueous pigment dispersions of this invention. Such components may also be conveniently included in the ante-colorized retardant solution.

It is important that the pigments of this invention remain dispersed as an emulsion, dispersion, or suspension. Accordingly, constituents that cause agglomeration should not be included, unless the agglomerating effects are effectively counteracted, in the flame retardant compositions used in this invention. For example, the presence of attapulgus clay in some fire retardant solutions leads to the agglomeration of some pigment dispersions. It is understood that it is the agglomeration that should be avoided rather than any particular ingredient. Thus, any potential agglomerating ingredient should be counteracted by any convenient effective dispersing ingredient such as, for example, a dispersing agent or a surfactant.

The fire retardant systems of the present invention can include conventional pigments supplemented by an aqueous emulsified or suspended copolymer/dye component (aqueous pigment dispersion colorant). When used as a supplemental colorant, the amount of the aqueous pigment dispersion colorant can be any convenient amount effective to provide the desired properties. In one example, about 0.35% by volume of the pigment dispersion improved the coloration of the ante-colorized fire retardant solution to an acceptable level.

The fire retardant system of the present invention can include any convenient opacifier such as, for example, titanium dioxide, potassium titanate, zinc oxide, zinc sulfide, lead salts, antimony oxide, earth-tone colored iron oxides, iron phosphates and the like, and selected extender or filler pigments such as non-reactive clays, calcium sulfate and mixtures thereof at a level effective to provide a desired amount of opacity. The opacifier can be any hiding pigment or any filler powder that (i) is insoluble and non-reactive in the fire retardant solution and (ii) becomes acceptably inconspicuous after the application of the fire retardant solution. It is preferred that the opacifier is able to opacify or hide the substrate without causing significant abnormal colors relative to the applied environment. Thus, for applications to forest fires, an earth tone would be desirable as a background color to which the colorized liquid fades. Such earth tones can be formed by using brown iron oxide with a white pigment to lighten the brown color as desired to blend with the background color of the area of dispersal as the fugitive color fades.

The color properties of the fire retardant system of the present invention increase with applied film thickness. The opacity (hiding power), the transmitted color intensity of the wet film, and the reflected color intensity of the dry film increase with coverage level. The fire retardant system of the present invention provides effective visibility at the coverage levels typically required in the field. For example, fire retardant coverage levels of the present invention equal to and above about 4 gpc (gallons per hundred square feet), (0.0014 M 3 /M 2 (M 3 fire retardant per M 2 area sprayed) or 1.4 L/M 2 (liters per square meter)), equivalent to an applied film greater than 0.064 inch (0.163 cm) thick, result in opaque films with the hiding equivalent of 1.0% iron oxide but with a considerably greater intensity of red. Such increased color is significant for use in fire situations such as, for example, in tall fuels where the fire retardant solution penetrates and covers the fuel complex from the tree crowns to the ground. This results in significantly less solution being visible on top of the tall fuel. In such situations, coverage levels above 4 gpc (1.4 L/M 2 ) are typically needed to control the fire. Hence, the color is correspondingly increased, thereby providing adequate visibility.

The aqueous pigment dispersion colorant utilized in the present invention can be a pigment comprising any convenient polymer, copolymer, terpolymer, or multipolymer blends incorporating any convenient non-fluorescent or fluorescent dye. For example, an aqueous dispersion of non-fluorescent or fluorescent pigments similar to those described in U.S. Pat. Nos. 5,294,664 and 5,215,679, can be used.

The aqueous pigment dispersion colorant employed by the present invention is an emulsion or suspension of a pigment having any convenient particle size effective to provide the necessary emulsion or suspension properties and the necessary coloration properties. In general, smaller size and higher surface area are desirable. In one embodiment, the pigments have average particle diameters of less than about 10 micrometers. In another embodiment, the pigments have average particle diameters of less than about 5 micrometers. In yet another embodiment, the pigments have average particle diameters of less than about 1 micrometer. For example, when the pigments described in U.S. Pat. Nos. 5,294,664 and 5,215,679 are used, it is preferred that the pigment has an average particle size from about 0.01 μm to about 1 μm. The aqueous dispersion can include anionic surfactants, opacifiers, extenders, dispersant and/or other functional components to enhance performance.

An example of this invention utilizes a pigment that is a polymer formed from at least four monomers: a water insoluble non-polar vinyl monomer which is advantageously styrene; a vinyl monomer containig sulfonate groups which is advantageously sodium 2-acrylamido -2-methylpropane-sulfonate; a polar vinyl monomer which is advantageously hydroxypropyl methacrylate, vinyl acetate, a polar, nonchlorinated, nonepoxidized acrylate ester, or a substituted acrylamide containing hydroxyl or carboxylic ester groups; and a vinyl nitrile which is advantageously acrylonitrile.

The fluorescent pigment that can be used in this invention includes any convenient powder incorporating any convenient fluorescent dye such as, for example, benzothioxanthene, xanthene, coumarin, naphthalimide, benzoxanthene, perylene, and acridine. The dye can be water soluble or insoluble, anionically or cationically charged, or nonionic.

The non-fluorescent pigment that can be used in this invention includes any convenient powder, effective to form an aqueous dispersion, incorporating any convenient non-fluorescent dye such as, for example, those dyes described in the Pigment Handbook, edited by T. Patton, Vol.1, Wiley-Interscience. The dye can be water soluble or insoluble, anionically or cationically charged, or nonionic.

The ante-colorized fire retardant solution to which the aqueous pigment dispersion colorant of this invention is added can be formed by any convenient method such as (i) by mixing a dry powder fire retardant formulation with water, or (ii) by mixing a fire retardant fluid or liquid concentrate with water. As described above, the aqueous pigment dispersion colorant of this invention must not agglomerate when added to the ante-colorized fire retardant solution. Accordingly, the ante-colorized fire retardant solution should not have any agglomerating component such as, for example, attapulgus clay unless the agglomerating component's action is effectively counteracted.

Tests on the fire retardant solutions of the present invention showed that their viscosity stability, corrosivity, and pumpability would not present any problems to use. Further, tests on the freeze-thaw characteristics of the aqueous dispersion pigment showed that their freeze-thaw stability would not present any problems to use.

The Examples which follow are intended as illustrations of certain preferred embodiments of the invention, and no limitation of the invention is implied.

Examples 1-8, Comparative Examples C1-C5, and Comparative Examples OpC1-OpC6—Four Aqueous Pigment Dispersion Colorants

Nineteen examples of fire retardant solutions were made. The base uncolored fire retardant concentrate was PHOS-CHEKE® D-75, an uncolorized form of colorized PHOS-CHEK® D-75R or D-75F, made by Monsanto Company (St. Louis, Mo.). That is, PHOS-CHEK® D-75 colorized with the conventional STD pigment results in PHOS-CHEK® D-75F. PHOS-CHEK® D-75R is PHOS-CHEK® D-75 with red iron oxide added. The color pigments and opacifiers used in these samples are described in Table 1 below:

TABLE 1
STD                              Standard dry powder conventional fugitive pigment contain-
                                 ing a light sensitive dye and an opacifier in a polymer
                                 matrix, manufactured by Radiant Color Corporation
                                 (Richmond, California).
PMT1                             Fugitive pigment, conventional dry powder type,
                                 containing a light sensitive laked dye and an
                                 opacifier in a polymer matrix, prepared by
                                 Radiant Color Corp.
PINK                             Aqueous pigment dispersion, Aurora Pink Glo-
                                 Sperse Pigment Suspension from Day-Glo
                                 Color Corporation (Cleveland, Ohio).
RED                              Aqueous pigment dispersion, Rocket Red Glo-
                                 Sperse Pigment Suspension from Day-Glo Color Corp.
ORANGE                           Aqueous pigment dispersion, Blaze Orange Glo-
                                 Sperse Pigment Suspension from Day-Glo Color Corp.
CRIMSON                          Aqueous pigment dispersion, Crimson Splash
                                 Emulsified Pigment Suspension from Day-Glo
                                 Color Corp.
Micro-1                          Microspherical conventional dry powder pigment
                                 manufactured by Radiant Color Corp.
Micro-STD                        Microspherical dry powder pigment containing
                                 same dye as that in STD, manufactured by
                                 Radiant Color Corp.
TiO                                                                        2 Pigment grade titanium dioxide.
Fe                                                                        2                                                                    O                                                                        3 Red pigment grade iron oxide

The nineteen examples included uncolored, fugitive-colored, opacified fugitive-colored, and a non-fugitive-colored example. Examples 1-4 are non-opacified examples of the present invention utilizing the CRIMSON, PINK, RED, and ORANGE pigments, respectively. Examples 5-8 are opacified examples of the present invention utilizing the CRIMSON, PINK, RED, and ORANGE pigments, respectively. Comparative Examples C1-C4 contain different dry-powder type fugitive pigments in a non-opacified retardant solution for comparison utilizing the STD, PMT1, Micro-1, and Micro-STD pigments, respectively. Comparative Example C5 is a non-opacified, non-fugitive-colored example for comparison. Comparative Examples OpC1-OpC4 are opacified examples for comparison utilizing the STD, PMT1, Micro-1, and Micro-STD dry-powder type pigments, respectively, and can be considered opacified examples of the respective Comparative Examples C1-C4. Finally, Comparative Examples OpC5 and OpC6 are opacified non-fugitive-colored examples for comparison. The characteristics of the nineteen examples are summarized in Table 2 below:

	TABLE 2
			Aqueous
		Fugitive-	Emulsion or
	Opacified	Colored	Suspension
Examples 1-4	NO	YES	YES
Examples 5-8	YES	YES	YES
Comparative Examples	NO	YES	NO
C1-C4
Comparative Examples	YES	YES	NO
OpC1-OpC4
Comparative Example	NO	NO	NO
C5
Comparative Examples	YES	NO	NO
OpC5 and OpC6

In one study, the compositions described in Table 2 were prepared by adding the fugitive color pigment (both the dry powder and the aqueous pigment dispersions) to the uncolorized PHOS-CHEK® D-75 dry-powder concentrate. The resulting colorized dry-powder concentrates were then admixed with water to prepare the respective fire retardant solutions of each example. In a second study, the fugitive color pigments were added to the uncolorized PHOS-CHEK® D-75 fire retardant solution (i.e., after the uncolored dry-powder retardant had been dissolved in water at its recommended mix ratio).

Example 1 was formulated using an emulsified liquid, composed of a dyed copolymer in an aqueous media. The emulsified liquid was Crimson Splash Color (“CRIMSON”), made by Day-Glo Color Corp., Cleveland, Ohio, which had a specific gravity of 1.06 (equivalent to 8.8 pounds per gallon) and contained approximately 45% solids content and a volatile content of about 55%. The emulsion was made by polymerization of a mixture of an acrylonitrile-styrene hydroxypropyl-methacrylate monomers and a dye in an aqueous media. The emulsion can be formed by any convenient method such as, for example, in accordance with U.S. Pat. Nos. 5,294,664 and 5,215,679. Sodium tridecyl ether sulfate surfactant was added to the media to stabilize the suspension stability. The resultant polymer particles were spherical in shape and had a mean diameter in the range of from about 0.35 μm to about 0.40 μm. The surface area of the particles was about 13 to about 15 square meters per gram. No opacifiers were added.

Example 2 used Glo-Sperse Aurora Pink (“PINK”), a dyed copolymer in an aqueous media made by Day-Glo Color Corp. The dyed copolymer dispersion had similar properties as those of Example 1, i.e., about 8.8 pounds per gallon and about 45% active pigment concentration. No surfactant was used in addition to the PINK aqueous dispersion. The polymer particle mean diameter size was in the range of from about 0.45 to about 0.55 microns, resulting in a lower surface area from the particles used in the dispersion of Example 1.

Example 3 used Glo-Sperse Rocket Red Polymer (“RED”), a dyed copolymer in an aqueous media made by Day-Glo Color Corp. The dyed copolymer dispersion had similar properties as those of the dispersion used in Example 2. Glo-Sperse Rocket Red Polymer contained 0.48% C.I. Basic Red 1 dye together with unspecified amounts of Potomac Yellow (CAS No. 80100023-5009-P) and Sierra Yellow (CAS No. 80100023-5018-P).

Example 4 used Glo-Sperse Blaze Orange Polymer (“ORANGE”), a dyed copolymer in an aqueous media made by Day-Glo Color Corp. Example 4 differs from Example 3 by having only 0.28% C.I. Basic Red 1 dye.

Examples 1-4 are similar, differing only in the types and amounts of dyes and surfactants that are contained in their compositions and small differences in physical characteristics such as average particle diameter and surface area. The colors of the aqueous pigment dispersions included in these Examples can be described as follows: Example 1 exhibited a high intensity crimson color, Example 2 exhibited a considerably lighter pink color, Example 3 exhibited a red color having an intensity greater than that of Example 2 but less intense than Example 1, and Example 4 exhibited a color similar to International Orange. The colors can be characterized according to values of the parameters L, a, and b which are described further below. The data for L values are shown below in Table 9, the a value data are shown below in Table 10, and the b value data are shown below in Table 11.

In each of these examples, all the dry-powder components of the uncolored fire retardant concentrate were first admixed together while still dry and then mixed with rapidly agitated, room temperature water at a ratio of 1.2 pounds per gallon of water (0.144 grams per milliliter). The gum thickener component of the concentrate causes the viscosity of the solution to begin to increase shortly after wetting occurs and forms the base uncolored fire retardant solution. When a dry-powder pigment was incorporated into the Comparative Example formulations, it was added to the other dry-powder fire retardant components prior to mixing to form the fire retardant solution. On the other hand, when an aqueous pigment dispersion of the present invention was incorporated into the Example formulations, the ante-colorized fire retardant solution was prepared as illustrated in Table 3a below and, then the aqueous pigment dispersion was mixed therein.

	TABLE 3a
	Ex. 1	Ex. 2	Ex. 3	Ex. 4
	ppw	ppw	ppw	ppw
Uncolored Concentrate	111.8	111.8	111.8	111.7
FUGITIVE COLOR
CRIMSON	3.221
PINK		3.221
RED			3.221
ORANGE				3.278
TOTAL	115.048	115.048	115.048	115.048

The viscosities of the resultant colorized fire retardant solution examples were measured 10 minutes after beginning the final mixing procedure and after 32 days of ambient temperature storage. The measured viscosity data are shown in Table 3b below:

	TABLE 3b
	Ex. 1	Ex. 2	Ex. 3	Ex. 4
wt % Fugitive
pigment in
Aqueous Pigment	45.0	45.0	44.34	44.36
Dispersion
Fire Retardant	1.26	1.26	1.24	1.26
Concentrate
SOLUTION VISCOSITY (cps)
10 Min after mixing	1633	1633	1673	1613
32 Days after mixing	1553	1597	1607	1580
Δ change	80	66	66	33

Table 3b illustrates that the fugitive pigment content of Examples 1-4 are essentially identical.

The concentration of fugitive pigment in the fire retardant is calculated on the basis of the wt % present in the dry retardant concentrate and not on the total solution. As an example of the various wt % relationships, 25 pounds (11.37 kg) of standard fugitive color blended into 2000 pounds (909.8 kg) of fire retardant concentrate would lead to a concentration of 1.25% of the color in the resulting dry powder. Then, for example, 1.2 pounds (544.32 g) of the dry powder which contains 0.015 pounds (6.8 g) of fugitive pigment, can be mixed with a gallon (8.32 lb. or 3.785 kg) of water to produce the solution. The resulting solution would contain 0.0157% pigment solids (6.8/(3785+544.32)).

Examples 5-8 are opacified examples made similarly to Examples 1-4 except that 1.15 ppw of TiO 2 and 0.29 ppw of Fe 2 O 3 were added for opacification to each formulation of Examples 1-4. The opacifiers were added as dry powders to the other dry-powder components of the uncolored fire retardant concentrate and admixed together while still dry. The dry mixture was then mixed with rapidly agitated, room temperature water and the process continued as described above for Examples 1-4. The compositions of Examples 5-8, in parts per weight (ppw), and the measured viscosity data for each Example are shown in Table 4 below:

	TABLE 4
	Ex. 5	Ex. 6	Ex. 7	Ex. 8
	ppw	ppw	ppw	ppw
Uncolored Concentrate	110.0	110.0	109.9	109.9
FUGITIVE COLOR
CRIMSON	3.566
PINK		3.566
RED			3.624
ORANGE				3.624
OPACIFIER
TiO 2	1.150	1.150	1.150	1.150
Fe 2 O 3	0.288	0.288	0.288	0.288
TOTAL	115.048	115.048	115.048	115.048
% Fugitive
pigment in
Aqueous Pigment	45.00	45.00	44.34	44.16
Dispersion
Fire Retardant	1.26	1.26	1.24	1.26
Concentrate
% Opacifiers in	0.14	0.14	0.16	0.13
Fire Retardant
Concentrate
SOLUTION VISCOSITY (cps)
10 Min after mixing	1630	1673	1667	1630
32 Days after mixing	1550	1633	1600	1543
Δ change	80	40	67	87

Comparative Examples C1-C4 used conventional dry powder pigments as the fugitive colorants. These pigments were added to the uncolored base concentrate at the calculated concentration which resulted in a nominal pigment concentration in the dry powder component of 1.26%.

In each of the Comparative examples, all the dry-powder components (including the uncolored fire retardant concentrate and dry-color pigments). were first admixed together while still dry. This dry blend was then mixed with rapidly agitated, room temperature water at a ratio of 1.2 pounds per gallon of water (0.144 grams per milliliter). The viscosity of the mixture begins to increase shortly after wetting occurs because of a gum thickener in the mixture.

As described above for the Examples, the viscosity was measured at different time intervals. The compositions of Comparative Examples C1-C4, in parts per weight (ppw), and the viscosity data are shown in Table 5 below:

	TABLE 5
	Comp. Ex.	Comp. Ex.	Comp. Ex.	Comp. Ex.
	C1	C2	C3	C4
	ppw	ppw	ppw	ppw
Uncolored Concentrate	113.6	113.6	113.6	113.6
FUGITIVE COLOR
STD	1.438
PMT1		1.438
Micro-STD			1.438
Micro-1				1.438
TOTAL	115.048	115.048	115.048	115.048
% Fugitive
pigment in
Dry-Powder	100.0	100.0	100.00	100.00
Pigment
Fire Retardant	1.25	1.25	1.25	1.25
Concentrate
SOLUTION VISCOSITY (cps)
10 Min after mixing	1747	1743	1727	1633
32 Days after mixing	1580	1507	1533	—
Δ change	167	236	194	—

Comparative Example C1 used a standard dry-powder type fugitive color pigment (“STD”) made by Radiant Color. The pigment is characterized as incorporating a red dye similar to C.I. Solvent Red, and approximately 5 wt % of an opacifier such as titanium dioxide in a polymer by a static-bed polymerization process. After cooling, the glass-like mass was pulverized to a median particle size of about 5 to 10 microns and exhibited a Hegman grind gauge measurement in the range of 5.0 to.5.5. The surface area of the pigment was estimated to be in the range of about 0.5 square meter per gram.

Comparative Example C2 was made by a process similar to that of Comparative Example C1 except that a barium laked Red 2B dye was incorporated in the dry-powder pigment (“PMT1”) during manufacture in place of the standard dye of Comparative Example C1. The dry-powder pigment PMT1 was made by a process similar to that used to make the standard dry powder pigment STD. The particle size and surface area of PMT1 was similar to the STD standard dry-powder fugitive pigment.

Comparative Examples C3 and C4 were mixed similarly to Comparative Example C1. The dry-powder fugitive pigment included in Comparative Examples C3 and C4 were pigments described by the manufacturer as microspherical having particle sizes in the range of about 0.5 to 2.0 microns. The pigments differed from each other in the dye that was incorporated in the pigment. The microspherical pigment (“Micro-1”) used in Comparative Example C4 used a different dye from Comparative Example C1, while Comparative Example C3 used a microspherical pigment (“Micro-STD”) that incorporated the same dye that was in the STD standard dry powder pigment of Comparative Example C1.

Comparative Examples OpC1-OpC4 were the respective Comparative Examples C1-C4 opacified with an additional 1.3 ppw (1.0 wt %) titanium dioxide and 0.3 ppw (0.25 wt %) red iron oxide (Fe 2 O 3 ). The opacifiers were added as dry powders to the other dry-powder components of the base uncolored fire retardant composition, admixed, and added to water under agitation as described above.

viscosity measurements were performed similarly as described above. The compositions of Comparative Examples OpC1-OpC4, in parts per weight (ppw), and the viscosity data are shown in Table 6 below:

	TABLE 6
	Comp. Ex.	Comp. Ex.	Comp. Ex.	Comp. Ex.
	OpC1	OpC2	OpC3	OpC4
	ppw	ppw	ppw	ppw
Uncolored Concentrate	112.0	112.0	112.0	112.0
FUGITIVE COLOR
STD	1.611
PMT1		1.611
Micro-STD			1.611
Micro-1				1.611
OPACIFIER
TiO 2	1.150	1.150	1.150	1.150
Fe 2 O 3	0.288	0.288	0.288	0.288
TOTAL	115.049	115.049	115.049	115.049
% Fugitive
pigment in
Dry Powder	100.00	100.00	100.00	100.00
Pigment
Fire Retardant	1.26	1.26	1.24	1.26
Concentrate
% Opacifiers in	0.14	0.14	0.16	0.13
Fire Retardant
Concentrate
SOLUTION VISCOSITY (cps)
10 Min after mixing	1743	1693	1703	1580
32 Days after mixing	1543	1533	1567	—
Δ change	200	160	136	—

Comparative Example C5 was the standard uncolorized fluid and contained neither a fugitive pigment nor an opacifying component. Comparative Example OpC5 was an opacified version of Comparative Example C5 and contained 1.0 wt % titanium dioxide and 0.25 wt % red iron oxide. Comparative Example OpC6 is an example of a fire retardant concentrate that has a non-fugitive (“persistent”) color. Comparative Example OpC6 contained 1.0 wt % of the persistent red iron oxide in the fire retardant concentrate. In each case, the mixing procedure was similar to that described above.

Similarly, viscosity measurements were made as described above. The compositions of Comparative Examples C5, OpC5, and OpC6, in parts per weight (ppw), and the viscosity data are shown in Table 7 below:

	TABLE 7
	Comp. Ex.	Comp. Ex.	Comp. Ex.
	C5	OpC5	OpC6
	ppw	ppw	ppw
	Uncolored Concentrate	113.6	112.0	49.8
OPACIFIER
	TiO 2	—	1.150	—
	Fe 2 O 3	—	0.288	0.503
	TOTAL	113.610	113.438	50.331
	% Fugitive
	pigment in
	Dry Powder	0.00	0.00	0.00
	Pigment
	Fire Retardant	0.00	0.00	0.00
	Concentrate
	% Opacifiers	0.00	0.14	1.00
	and Persistent
	Color in
	Fire Retardant
	Concentrate
SOLUTION VISCOSITY (cps)
	10 Min after mixing	1617	1623	1700
	32 Days after mixing	—	—	—
	Δ change	—	—	—

The color and hiding ability (opacity) of each of the fire retardant solutions, prepared as described above, were characterized and compared using 4.0 inch wide films having a wet thickness of 0.032 inch that were drawn with an adjustable gap doctor blade on a standard glass plate. The films were allowed to dry for 20 minutes in a horizontal position prior to testing. The wet film thickness of 0.032 inch was equivalent to a fire retardant solution application rate in practice of 2 gpc (0.7 L/M 2 )

Light transmission through the fire retardant film for each formulation was measured on a HunterLab Ultrascan spectrocolorimeter. The measurements were made by Atlas Weathering Service Group's DSET Laboratories located at New River, Ariz. The Hunter Lab instrument had a six inch integrating sphere. Total transmittance was measured in accordance with ASTM D-2244-93 and ASTM E308-95 standards with a 10° observer and a D65 illuminant. The specimen port was circular and 1.00 inch in diameter with an 8° viewing angle and a beam diameter of 0.73 inch. Data reduction was computed from spectral data (X, Y and Z data points) taken every 10 nm over the wavelength range from 375 to 700 nm. The percentage of the illuminant light which passed through the film (Y) and its color were obtained on the wet film for each formulation at three times: about 20 and 120 minutes after application, and on the following morning prior to sunlight exposure.

The percentage of the illuminant light which passes through the film is directly related to the Y value obtained from the spectrocolorimeter; conversely, 100-Y is equivalent to the degree of opacification of the film. The L, a, and b color values were calculated from the above measurements. The (L) value is a measure of the lightness or darkness of the color, i.e., when L=100 the film is white, and when L=0 the film is black. Thus L=50 would be obtained for a film with equal amounts of black and white, i.e. a grey known in the graphic arts as 50% grey. The (a) value represents the red/green balance of the color, i.e., when (a) is positive, more red than green is present and when negative, more green than red is present. The greater the absolute value, the more intense the color. If (a)=0, neither red nor green is dominant over the other in the overall color. Similarly, the (b) value represents the yellow/blue balance of the film. When (b) is positive, the color contains more yellow than blue, when negative, the color contains more blue than yellow. Again, the greater the absolute value, the more intense the color. As examples of the effect of the interaction between (a) and (b), a color purple would have a high positive (a) value and a large negative (b) value resulting in a perceived combination of red and blue, while a color orange would have a mixture of positive (a) and positive (b) values that results in a perceived combination of red and yellow.

The L, a, and b values of light reflected from the test films were measured with a Hunter Lab Labscan spectrocolorimeter with 0°/45° geometry in accordance with STM D2244-93 and ASTM E308-90 standards with a 10° observer and D65 illuminant. The incident light was at a 0° angle and the viewing light was 45° relative to the specimen. The specimen port was circular and 1.00 inch in diameter. Data reduction was computed from spectral data taken every 10 nm over the wavelength range from 400 nm to 700 nm. In all cases the glass plate on which the test film was placed was backed with a forest green ceramic tile at the time of measurement. Measurements were made prior to exposure (at 0 Langleys exposure) followed by measurement at 6,000, 12,000 and 18,000 Langleys (2.51, 5.02, and 7.53×10 8 J/M 2 ) of natural sunlight exposure. In some cases, measurements were continued at 24,000, 33,000 and 36,000 Langleys (10.04, 13.8, and 15.06×10 8 J/M 2 ). Between light reflectance measurements the dry films were exposed to natural sunlight near Phoenix, Ariz. The films were exposed in accordance with ASTM G-24-87, Method A, using a tilt angle of 45° from the horizontal. The films were placed under glass to protect them from the effects of debris and rain. The films on the glass plates faced south with the plates mounted in a cabinet, with passive ventilation, unbacked, in aluminum frames. The mounted plates were removed from the racks and taken indoors for measurement. They were kept indoors in a dark environment during measurement and until a decision was reached as to whether any additional exposure was needed. In most cases, photographs were taken prior to exposure and at each exposure interval after measurements were made. An average of 360 Langleys (0.150×10 8 J/M 2 ) per day were accumulated. Accordingly, about 50 days of exposure was required to reach 18,000 Langleys (7.53×10 8 J/M 2 ).

The data obtained during this study are presented in Tables 8-11 below. Table 8 illustrates the performance of the various color pigments in a non-opacified film. A non-fugitive colorized formulation, Comparative Example OpC6, containing only 1.0 wt % red iron oxide was exposed in the same manner as the fugitive colorized films to identify differences in color composition, color intensity and fading. Example 5, an opacified example, is also included to show the increased opacity of the opacified Example.

The viscosity data at the bottom of Tables 3-7 reveal that the Comparative Examples lost an average of 10% (range 7.6 to 13.4%) of their 10 minute viscosity when stored at ambient temperature for one month. The examples of the present invention, on the other hand, lost an average of only about 4% (range 2.0 to 5.3%) of their 10 minute viscosity during this same storage period.

Generally, uncolorized fire retardant solutions exhibit lower viscosity stability than the same formulation containing a colorizing pigment. Fugitive-colorized fire retardants are more stable than uncolorized fire retardant solutions and persistent iron oxide non-fugitive colorized fire retardant solutions are the most stable. It is believed that the color components in a solution alter the spectral properties and the penetration depth of light impinging on the solution, thereby mediating the overall impact of the impinging light on the solution. The Examples of the present invention were somewhat more stable than the Comparative Examples.

The aerial visibility of a fire retardant film is believed to be significantly influenced by the hiding ability of the film—that is, the ability of the film to hide that on which it is placed. The hiding ability is related to the film's opacity. One measure of the hiding ability of a film is determining the percentage of applied light which is transmitted through the fire retardant film. Smaller values indicate less light transmission which corresponds to increased opacity and better hiding ability.

Film transparency decreases (opacity increases) during drying due to the precipitation of soluble components as the solvent (water) evaporates. The percentage of light transmitted through the non-opacified Examples 1-4, the non-opacified Comparative Examples C1-C5, the Comparative Example red iron oxide formulation OpC6, and the opacified Example 5 were measured and are shown in Table 8 below:

	TABLE 8
	Light transmission (%)
	WET	DRY
	Comparative Example C5	85	65
	Comparative Example C1	62	45
	Comparative Example OpC6	28	22
	Comparative Examples C2-C4	57-69	41-50
	Examples 2-4	58-60	47-52
	Example 1	43	39
	Example 5	17	17

The hiding efficiency of a pigment is the difference between the transparency of the fire retardant formulation containing the pigment and one containing no pigment, i.e., Comparative Example C5. This difference between the standard fugitive colorized Comparative Example C1and the standard non-fugitive iron oxide colorized Comparative Example OpC6 is dramatically illustrated by the above data. Comparative Example OpC6 is shown by the above data to block approximately twice as much light as Comparative Example C1, both when wet and when dry.

Examples 2-4 did not show significant improvement over the standard pigment Comparative Example C1in terms of either wet or dry film transparency, i.e., increased opacity. Example 1, however, offered significantly improved wet film opacity and somewhat superior dry film opacity relative to the other non-opacified fugitive pigment-containing formulations (Examples 2-4 and C1-C4). Example 5 illustrates the dramatic improvement possible by the inclusion of opacifiers in the film.

As described above, the L value relates to the lightness or darkness of the film, i.e., black and white have L values of 0 and 100 respectively. Table 9 below shows the L values for the fire retardant films included in these experiments. Both wet and dry measurements were made of the color transmitted through the film. The color of the light reflected from the films was measured only after drying. Comparison should not be made between reflected and transmitted color measurements, i.e., comparison should be made only within a given column or measurement method.

	TABLE 9
		Reflected
	Transmitted Light (%)	Light (%)
	Wet	Dry	Dry
Comparative Example C5	93	84	59
Comparative Example C1	83	73	49
Comparative Example OpC6	61	22	42
Comparative Examples C2-C4	81-87	70-76	50-55
Examples 2-4	81-83	74-77	54-66
Example 1	72	69	46

The 1.0% iron pigment in Comparative Example OpC6 darkens the film significantly more than 1.25% of any of the fugitive color pigments. It should be pointed out, as described earlier, that the levels of fugitive color pigments are recited as wt % taken back to the powder, without liquid components, in order to make consistent comparisons with the comparative examples that are made from dry powders. The comparison examples cannot form dispersions—accordingly, as described earlier, the % of fugitive color pigment in the liquid is not comparable to the % of fugitive color pigment in the dispersion.

Example 1 showed greater increase in film darkening than the other fugitive colorants, although not to the same extent as iron oxide. The desirability of having a light or dark film is dependent on the fuels on which the film solution is being used. Light colors would be expected to be more visible on dark green timber while dark colors would be more visible on light colored fuels such as leaves and grass.

As described above, the (a) value relates to the relative intensities of red and green. Positive values indicate the dominance of red, negative numbers indicate the dominance of green. Table 10 shows the measured (a) values for the films. The data shows that uncolorized Comparative Example C5 has a greenish cast which changes to red upon the introduction of pigment.

Several of the fugitive pigments are shown in Table 10 to provide a more intense or brilliant red color than the non-fugitive red iron oxide Comparative Example OpC6. Examples 2-4 appeared to be at least about equivalent to iron oxide in terms of red intensity. Example 1, however, was the best of the formulations. It provided greater red-intensities under both wet and dry conditions.

	TABLE 10
	Transmitted Light
	(%)	Reflected Light (%)
	Wet	Dry	Dry
Comparative Example C5	−2	−2	−5
Comparative Example C1	8	12	16
Comparative Example OpC6	12	18	25
Comparative Examples C2-C4	3-12	8-16	11-29
Examples 2-4	10-16	12-20	25-29
Example 1	21	24	30

As described above, the (b) value relates to the relative intensities of yellow and blue. Positive values indicate the dominance of yellow while negative values indicate the dominance of blue. Again, larger absolute numbers indicate higher intensities. Table 11 below shows the (b) values measured for the tested films.

	TABLE 11
		Reflected
	Transmitted Light (%)	Light (%)
	Wet	Dry	Dry
Comparative Example C5	2	7	3
Comparative Example C1	5	12	10
Comparative Example OpC6	6	18	25
Comparative Examples C2-C4	3	8-16	11-29
Examples 2-4	−5 to −20	12-20	25-29
Example 1	2	24	30

As described previously, pigments containing high levels of red visually tend towards orange when the b value is positive, and purple when the b value is negative.

The film of uncolorized Comparative Example C5 darkened (decreasing L value) while changing only slightly in other color properties after exposure to natural sunlight. The fugitive pigment candidates tended to darken somewhat with exposure as well. The red content of the fugitive pigments faded during sunlight exposure. The standard Comparative Example C1lost essentially all of its red color within 6,000 Langleys (2.51×10 8 J/M 2 ) of sunlight. The rate of “red” fade varied significantly from candidate to candidate.

The opacified films were identical to the non-opacified films except that the increased level of hiding pigment improved-their ability to hide the substrate on which they were applied. The composition of these formulations are shown in Tables 4, 6, and 7 above. Titanium dioxide whitens the films. Small concentrations of red iron oxide mixed with the white titanium dioxide resulted in a non-pigmented film being colored somewhere between pink and tan. Slightly higher levels of fugitive pigment were used in the opacified films in order to offset the tendency of the opacifier agents to produce pastels.

With respect to hiding ability, opacified Comparative Example OpC5 film containing no fugitive color transmitted 28% and 25% of the illuminant's light through the wet and dry film respectively. These light transmission values were almost identical to those observed with Comparative Example OpC6 which was pigmented with just red iron-oxide (28% and 22% respectively). Accordingly, the opacification was equivalent to iron oxide in terms of hiding ability even without a fugitive pigment component. The non-opacified film Comparative Example C5, on the other hand, transmitted 85% and 65% of the transmitted light. Inclusion of the fugitive pigments reduced light transmission even further resulting, in all cases, in hiding abilities superior to red iron oxide. Opacified Example 5 was superior to all the other fugitive pigmented formulations in hiding ability.

With respect to L value, based on light transmission measurements, the opacified, but uncolorized, Comparative Example OpC5 film had light/dark characteristics when wet similar to the equivalent film, Comparative Example OpC6, that contained only the 1.0% red iron without the TiO 2 . Based on reflected light measurements, however, the dry Comparative Example OpC5 film was considerably lighter then the Comparative Example OpC6 film that contained iron oxide. This was consistent with visual observation. The fugitive pigments appeared to darken the opacified films only slightly and all remained considerably lighter than the Comparative Example OpC6 films that contained just the non-fugitive-colorant red iron oxide.

With respect to (a) and (b) values, the opacified but uncolorized Comparative Example OpC5 film had considerably more red and yellow in it than the non-opacified Comparative Example C5 equivalent. This is to be expected since red iron oxide contains high levels of both these colors. This increase in red and yellow carried through to the colors of the films containing fugitive pigments. In most cases, the fugitive colorized films contained a more intense red color than iron-oxide. Example 1 was superior to the others although, in opacified films, all of the pigments were at least equivalent in visibility to iron oxide.

With respect to fading, when incorporated into opacified formulations, the fugitive color pigments faded in the same manner as the non-opacified formulations. However, color emanating from the non-fugitive opacifiers, red iron oxide and titanium dioxide, did not fade. These formulations therefore inherently had background colors. As would be expected, such opacified formulations faded only to their background colors. Examples 9-23, Comparative Examples C6-C13, and Comparative Examples OpC13-OpC15—Pigment Concentrations:

Examples 9-23 were formulated to investigate the effect of pigment and opacifier concentration when used individually and in combination with each other. The formulations were made using the PHOS-CHEK® D-75 fire retardant and modifications thereto.

The formulations are shown in Table 12 below:

	TABLE 12
	Formulation	#
	PHOS-CHEK ® D-75	1.25% STD	C6
	Containing	1.50% STD	C7
		1.75% STD	C8
		2.00% STD	C9
	D-75 with STD replaced by	1.50% PMT1	C10
		1.75% PMT1	C11
		2.00% PMT1	C12
	D-75 having 1.25% STD and	0.31% CRIMSON	9
		0.63% CRIMSON	10
		0.94% CRIMSON	11
	D-75 (without STD) with	0.0% CRIMSON	C13
	added	0.90% CRIMSON	12
		1.13% CRIMSON	13
		1.35% CRIMSON	14
		1.58% CRIMSON	15
	D-75 (without STD) with	0.0% CRIMSON	OpC13
	0.5% TiO 2 and	0.90% CRIMSON	16
		1.13% CRIMSON	17
		1.35% CRIMSON	18
		1.58% CRIMSON	19
	D-75 (without STD) with	0.0% CRIMSON	OpC14
	1.0% TiO 2 and	0.90% CRIMSON	20
		1.13% CRIMSON	21
		1.35% CRIMSON	22
		1.58% CRIMSON	23
	D-75 and	1.0% Fe 2 O 3	OpC15

Note that the percentages provided in Table 12 are percentages of the dry formulation—that is, as described above, weight percent of the formulations without any liquid. Thus, for the comparative examples the weight percentages describe the actual weight percent of the colorant added and present in the dried film. However, the dispersions of the invention are about 45% active by weight of the aqueous dispersion, with 55% media. Accordingly, the weight percent added in terms of the dispersions that contained the CRIMSON added to the total fire retardant was 2.22 times the percent shown in Table 12. That is, 0.31 wt % CRIMSON corresponds to adding 0.68 wt % of the aqueous color dispersion containing the CRIMSON, 0.63 wt % CRIMSON corresponds to adding 1.40 wt % of the aqueous color dispersion containing the CRIMSON, 0.90 wt % CRIMSON corresponds to adding 2.0 wt % of the aqueous color dispersion containing the CRIMSON, 0.94 wt % CRIMSON corresponds to adding 2.08 wt % of the aqueous color dispersion containing the CRIMSON, 1.13 wt % CRIMSON corresponds to adding 2.5 wt % of the aqueous color dispersion containing the CRIMSON, 1.35 wt % CRIMSON corresponds to adding 3.0 wt % of the aqueous color dispersion containing the CRIMSON, and 1.58 wt % CRIMSON corresponds to adding 3.5 wt % of the aqueous color dispersion containing the CRIMSON.

The preparation of the films of the above Examples 9-23 of the present invention were made similarly to the procedures described previously for Examples 1-8. The preparation of the films of the above Comparative Examples C6-C13, and OpC13-OpC15 were made similarly to the procedures described previously for Comparative Examples C1-C5, and OpC1-OpC6 as appropriate. The testing and data collection procedures were also similar to those described previously.

The data obtained in this study are shown in Tables 13 and 14A-14C. The amount and red color intensity of the light transmitted through the wet and freshly dry film and the initial reflectance data are shown in Table 13. Tables 14A-14C tabulate the degree of fading experienced after 6,000, 12,000 and 18,000 Langleys (2.51, 5.02, and 7.53×10 8 J/M 2 ) of natural sunlight exposure. Exposure was conducted during March and April, 1997 at New River, Ariz.

	TABLE 13
	Transmission Through Fresh Film
	Active Pigment Content (% of	% Transmission	(a) Red Intensity**	Reflectance - Fresh, Dry Film
#	dry retardant concentrate)	wet	dry	wet	dry	L Value †	(a) Value**	(b) Value +
OpC15	1.00	31.4	16.5	10.4	17.0	42.4	25.7	18.1
C6	1.25	63.2	36.5	7.3	10.9	50.8	15.4	9.1
C7	1.50	60.6	34.9	8.3	13.7	50.0	18.7	12.5
C8	1.75	57.8	34.0	9.2	15.3	50.4	21.1	13.9
C9	2.00	58.1	35.0	9.4	14.2	50.5	21.5	14.7
C10	1.50	56.6	31.6	8.7	14.1	49.0	20.6	7.4
C11	1.75	57.1	33.9	7.6	12.3	50.1	20.1	7.3
C12	2.00	52.4	30.7	11.0	15.3	47.0	23.4	8.6
9	1.56	54.0	36.0	11.6	16.0	47.6	23.0	10.1
10	1.88	44.7	29.3	17.8	22.3	47.8	29.9	12.6
11	2.19	40.6	27.4	24.0	26.2	47.1	32.9	13.4
C13	0.00	84.9	57.1	−2.5	−3.7	59.9	−5.7	4.3
12	0.90	52.8	37.0	12.9	16.7	48.0	26.0	6.6
13	1.13	48.9	34.0	16.2	21.5	47.3	30.9	9.2
14	1.35	40.9	32.4	21.8	23.8	48.1	34.0	10.4
15	1.58	36.7	29.7	26.6	28.8	47.0	37.0	12.7
OpC13	0.50	57.9	42.3	−1.7	−2.7	65.6	−5.2	2.6
16	1.40	32.4	25.3	19.4	23.0	54.3	28.4	6.3
17	1.63	26.5	20.2	25.5	30.4	53.3	32.1	7.7
18	1.85	25.5	20.8	26.0	30.0	52.5	34.4	8.9
19	2.08	24.1	21.2	32.5	32.3	51.6	37.7	10.9
OpC14	1.00	43.2	35.4	−1.8	−2.7	69.0	−5.1	2.4
20	1.90	23.8	19.6	23.1	24.7	57.5	27.1	4.8
21	2.13	23.9	18.8	26.3	27.0	57.2	30.5	6.0
22	2.35	18.5	16.8	31.2	32.3	54.6	33.2	7.2
23	2.58	18.6	16.6	34.8	33.9	53.9	35.9	8.7
	Background tile - no fire retardant film		20.4	−19.2	3.6

	TABLE 14A
	Active Pigment	Reflectance - 6K Langleys
	Content (% of	(2.51 × 10 8 J/M 2 )
	dry retardant		(a)	(b)
#	concentrate)	L Value†	Value**	Value+
OpC15	1.00	43.6	24.6	16.9
C6	1.25	59.6	1.2	5.7
C7	1.50	58.9	0.6	8.4
C8	1.75	60.1	−0.1	8.4
C9	2.00	59.3	1.2	10.9
C10	1.50	49.9	17.5	6.6
C11	1.75	50.3	16.9	6.8
C12	2.00	47.2	20.1	8.0
9	1.56	56.1	7.0	7.1
10	1.88	57.3	13.0	8.7
11	2.19	56.6	16.9	8.9
C13	0.00	56.6	1.0	6.0
12	0.90	53.3	14.1	7.9
13	1.13	52.5	18.0	9.9
14	1.35	54.3	21.8	10.5
14	1.58	53.6	24.8	11.8
OpC13	0.50	64.6	−0.5	2.7
16	1.40	60.4	16.4	7.5
17	1.63	60.2	20.1	8.3
18	1.85	59.8	22.7	9.3
19	2.08	59.5	27.1	10.5
OpC14	1.00	67.9	−0.7	2.1
20	1.90	64.5	16.2	6.1
21	2.13	65.0	19.5	6.8
22	2.35	61.8	21.3	8.1
23	2.58	61.0	24.5	9.0
Background tile - no	20.4	−19.2	3.6
fire retardant film

	TABLE 14B
	Active Pigment	Reflectance - 12K Langleys
	Content (% of	(5.02 × 10 8 J/M 2 )
	dry retardant		(a)	(b)
#	concentrate)	L Value†	Value**	Value+
OpC15	1.00	40.7	20.3	15.4
C6	1.25	51.1	−2.5	5.5
C7	1.50	57.5	0.8	10.7
C8	1.75	58.6	−0.1	10.9
C9	2.00	56.9	1.7	13.1
C10	1.50	50.3	14.3	8.0
C11	1.75	50.2	13.6	8.5
C12	2.00	47.1	16.8	9.4
9	1.56	49.2	−0.8	5.8
10	1.88	49.6	1.2	6.3
11	2.19	51.3	3.5	6.8
C13	0.00	55.1	−2.6	4.0
12	0.90	49.1	0.7	4.5
13	1.13	48.8	2.1	5.1
14	1.35	49.3	3.7	5.4
14	1.58	49.3	5.4	6.3
OpC13	0.50	57.3	−3.1	1.7
16	1.40	56.9	2.7	3.9
17	1.63	59.1	5.2	4.9
18	1.85	57.1	6.6	5.3
19	2.08	59.3	9.4	6.1
OpC14	1.00	62.3	−2.9	1.2
20	1.90	63.0	3.8	3.4
21	2.13	62.9	5.5	3.5
22	2.35	62.4	7.6	5.1
23	2.58	62.6	9.4	5.6
Background tile - no	20.4	−19.2	3.6
fire retardant film

	TABLE 14C
	Active Pigment
	Content (% of	Reflectance - Fresh, Dry Film
	dry retardant		(a)	(b)
#	concentrate)	L Value†	Value**	Value+
OpC15	1.00	42.0	20.0	15.5
C6	1.25	51.6	−1.9	7.4
C7	1.50	57.6	1.0	12.8
C8	1.75	58.8	0.1	13.3
C9	2.00	56.7	1.9	15.2
C10	1.50	52.4	11.0	9.8
C11	1.75	52.4	10.2	10.8
C12	2.00	48.9	13.5	11.5
9	1.56	49.9	−1.1	7.4
10	1.88	50.4	−0.3	7.5
11	2.19	52.2	0.9	7.8
C13	0.00	55.4	−1.8	5.7
12	0.90	49.8	−1.0	5.3
13	1.13	49.6	−0.3	5.5
14	1.35	50.3	0.5	5.5
14	1.58	50.3	1.3	6.1
OpC13	0.50	57.0	−2.3	4.1
16	1.40	57.0	0.1	4.9
17	1.63	59.4	1.4	5.7
18	1.85	57.9	2.1	5.8
19	2.08	60.2	3.4	5.8
OpC14	1.00	61.4	−2.1	3.5
20	1.90	63.0	0.6	4.7
21	2.13	63.3	1.3	4.4
22	2.35	62.8	2.8	5.6
23	2.58	63.0	3.8	5.7
Background tile - no	20.4	−19.2	3.6
fire retardant film
**As described previously, positive (+) values indicate red color, negative (−) values indicate green color, and higher numbers denote a greater intensity.
†When the L value = , the color is black, when the L value is 100, the color is white.
+As described previously, positive (+) values indicate blue color, negative (−) values indicate yellow color, and higher numbers denote a greater intensity.

PHOS-CHEK® D-75 containing added 1.25% STD fugitive powder pigment, Comparative Example C6, is a standard fire retardant solution. Increasing the concentration of the STD pigment to levels as high as 2.0% resulted in only minor improvements in the hiding ability and red intensity of the wet film, as shown by examination of Comparative Examples C6-C9. No improvement in hiding performance was seen in the dry film although the red intensity increased to nearly the level exhibited by a PHOS-CHEK® fire retardant prepared from a dry-powder concentrate containing 1.0 wt % red iron oxide. Thus, the data shows that the red iron oxide (Comparative Example OpC15) was superior to the formulation colored with 2.0% STD dry-powder fugitive pigment (Comparative Example C9) when compared in both the wet and dry films.

The Radiant Color PMT1 pigment's performance, at equal concentration, was somewhat superior to the standard fugitive color STD's performance in both the hiding ability and in the red intensity of the wet film. Neither property was significantly different from that of STD in the dry film, however, as shown by examination of Comparative Examples C6-C12.

In the case of Examples 9, 10, and 11, standard PHOS-CHEK® D-75 retardant concentrate containing 1.25% STD dry-powder fugitive pigment was used as the base material. CRIMSON was added to the D-75/1.25% STD solution at dry-pigment added levels of 0.31, 0.63 and 0.94 wt. % based on the amount of contained fugitive pigment in the CRIMSON liquid dispersion. This was equivalent to a 25, 50 and 75% increase in pigment solids relative to the standard D-75/1.25% STD product. This is also equivalent to 0.68, 1.40 and 2.08% of the liquid dispersion added to D-75 containing the standard 1.25% amount of STD. Similarly to the previous Examples of this invention, the aqueous fugitive-color CRIMSON suspension was added into the mixed D-75 solution and not to the dry D-75 powder.

While very significantly improving the hiding ability of both the wet and dry film, the highest level used in this study did not reach the level of hiding ability of 1.0% red iron oxide. On the other hand, the red intensity of the formulations were superior to 1.0% iron oxide at the intermediate addition concentration, i.e., 1.40% CRIMSON suspension addition. Further, the rate of fade of this mixture was slower than the standard color but nonetheless rapid enough to pass the U.S. Forest Service requirements. A somewhat slower rate of fade relative to the current STD pigment is believed advantageous in order to assure that fade does not occur during that period of time when visibility is desired.

In Examples 12-15, the CRIMSON pigment dispersion was added to the basic uncolorized D-75 solution (without the STD powder pigment) at concentrations of 2.0, 2.5, 3.0 and 3.5% of the dry-powder used to prepare the fire retardant solution—that is, 2.0, 2.5, 3.0 and 3.5% by weight of the dry ingredients. Only 2.0% (0.9% pigment solids) of the CRIMSON suspension was necessary to provide the red color intensity of the Comparative Example OpC15 (PHOS-CHEK® D-75 having additional 1% iron oxide). However, it is estimated that 4.0% (1.8% pigment solids) CRIMSON would be required to provide opacification equal to Comparative Example OpC15. The rate of fade of Examples 12-15 were adequate to meet U.S. Forest Service requirements.

Example 16 containing 2.0% CRIMSON (0.9% pigment solids) exhibited equivalent wet opacification and considerably greater red intensity than the standard 1.0% red iron oxide Comparative Example OpC15. Somewhat higher concentrations of CRIMSON would be required to obtain an opacity level superior to red iron oxide.

Example 20 containing 2.0% CRIMSON (0.9% pigment solids) exhibited wet opacification and red intensity considerably superior to 1.0% red iron oxide Comparative Example OpC15. It is believed that this formulation would be considerable more visible from the air than Comparative Example OpC15, although the additional titanium dioxide tended to reduce red intensity, i.e., make the color more pastel.

Examples 24 and 25, Comparative Examples C16-C18—Coverage Level

These formulations illustrated the impact of fire retardant solution coverage (application) level on the opacity and color characteristics of films. The previous experiments provided data from 0.032 inch (0.081 cm) thick wet films of the various formulations. That film thickness is equivalent to a fire retardant solution coverage level of 2.0 gpc (0.7 L/M 2 ). Standard PHOS-CHEK® D-75 containing 1.25% STD (based on the dry-powder retardant weight) is sufficiently visible when applied on light (yellow, tan and light to deep green) fuels of moderate height at application rates as low as 2 gpc (0.7 L/M 2 ). In some cases, however, solutions prepared with this formulation are difficult to see when the application is made to dark green, tall timber fuel types even when the coverage level is considerably higher, such as 8 gpc (2.8 L/M 2 ). In these latter cases, the fuel color can appear to be very dark, bordering on black, dependent on the amount of sunlight and the direction of approach. A further problem is that, when applied in tall timber, the solution penetrates through the forest canopy. That portion of the solution which does not lie on top of the forest canopy is, therefore, at least partially obscured from view from above. Accordingly, the standard formulation can be improved—particularly for uses where the solution is applied to tall and dark colored fuel types.

The formulations in this test series are shown in Table 15 below. Film thicknesses of 0.022, 0.032, 0.064, and 0.128 inches (0.056, 0.081, 0.163, and 0.325 cm) were prepared. However, it was observed that films thicker than about 0.032 inch (0.081 cm) continued to flow after application for the standard D-75 formulation. Such after-flow resulted in varying and unknown thicknesses within a given draw down for the test films prepared with the standard D-75 solution. To compensate for this, an increased amount. of guar gum thickener was used in the composition in order to increase the viscosity of the solution and thereby reduce after-flow. Comparative Example C16 is standard PHOS-CHEK® D-75 retardant solution prepared with a dry-powder formulation containing 1.25% STD at the standard viscosity. Comparative Example C17 is identical to Comparative Example C16 except that the amount of guar gum thickener was increased to 7.25% This resulted in a solution viscosity for Comparative Examples C17 and C18, and Examples 24 and 25 of about 2660 cps.

Comparison of Comparative Example C16 with Comparative Example C17 showed that the modification made to viscosity had no significant impact on light transmission and color characteristics.

Three fugitive pigments were included in this study, i.e., the STD standard dry pigment, the PMT1 standard dry pigment, and the CRIMSON aqueous color pigment dispersion of the present invention. Example 24 used CRIMSON to enhance the color of the existing (Agency qualified) PHOS-CHEK® D-75 with additional 1.25% STD and consequently contained a higher total pigment loading than the other formulations.

	TABLE 15
		Comp. Ex.	Comp. Ex.		Ex. 25
	Comp. Ex.	C17	C18	Ex. 24	(Uncolored D-75
	C16	(Comp. Ex.	(D-75 containing	(Comp. Ex.	solution containing
	(D-75	C16 with	1.25% PMT1 with	C17 with	2.78% CRIMSON
	containing	Increased	Increased	0.7%	and Increased
	1.25% STD)	Viscosity)	Viscosity)	CRIMSON	Viscosity)
Viscosity	1667	2660	2660	2667	2883
(cps)
	(%)	(%)	(%)	(%)	(%)
Guar	6.00	7.25	7.25	7.25	7.25
Fugitive Color
STD	1.25	1.25		1.25
PMT1			1.25
CRIMSON				0.70	2.78
% Active	1.25	1.25	1.25	1.56	1.25
Color

The films were prepared in the similar manner as described previously except the gap in the doctor blade was adjusted to provide wet film thicknesses of 0.022, 0.032, 0.064 and 0.128 inches (0.056, 0.081, 0.163, and 0.325 cm). The thinnest film (0.022 inch, 0.056 cm) is considered too thin for practical use in any but the least severe fire situations, but was included in the experimentation since that is the standard thickness used in the U.S. Forest Service test protocols for evaluating fugitive color fading. Film thicknesses of 0.032 and 0.064 inches (0.081 and 0.163 cm), were chosen to more closely represent real world application rates (2 and 4 gpc, or 0.7 and L/M 2 ). The 0.128 inch (0.325 cm) thick films flowed to some extent even at the higher viscosity level. In view of this, actual film thicknesses were not known and color quantification measurements not made. If should be noted, however, that this thick film corresponds to an 8 gpc (2.8 L/M 2 ) application rate which is reasonable for application on to tall timber areas of greatest concern relative to fire retardant visibility.

The data development techniques used in this study were similar to those described earlier except that, in some cases, reflected light measurements were made on both the top and bottom (through the glass) of the test films. This was done because it was observed that, in the thicker films, fading occurred from the exposed top through the film.

Sunlight exposure measurements were recorded during this study series. The test film plates were placed on the exposure stand on Mar. 31, 1997. The rates of exposure during the exposure period were as follows:

		Total Exposure	Average Rate
	Date	(Langleys)	(Langleys/day)
	Mar. 31, 1997	0
	Apr. 14, 1997	6,000	429
	May 02, 1997	12,000	444
	May 27, 1997	18,000	450
	Jun. 19, 1997	24,000	444

The data obtained during this study are shown in Tables 16, 17, 18A-18D and 19A-19C. Table 16 illustrates the percentage and color of the light which was transmitted through the wet film. As might be expected, these data show that the percent of light transmitted through the film decreased (opacity increased) and the intensity of the color increased with film thickness or coverage level. Table 17 illustrates the changes in light transmission and color intensity which occurred during drying of the fire retardant film. Light transmission decreased (opacification increased) as the film dried. It is believed that this is due to the precipitation of the dissolved solids as the solvent evaporated. The data indicate, as well, that color intensified during drying. This was inconsistent with the visual appearance of the film in that the film appeared to become more pastel as it dried. Tables 18A-18D illustrate the rate of fading of the various films and thicknesses of films during exposure to natural sunlight. These characteristics were measured initially and after exposures of 6K, 12K, 18K, 24K, and 30K Langleys (2.51, 5.02, 7.53, 10.04, and 12.55×10 8 J/M 2 ). The data from the unexposed values in Tables 18A-18D showed that little change in color intensity occurred as the film thickness was increased beyond about 0.064 inch (0.163 cm).

	TABLE 16
	Comp. Ex.	Comp. Ex.	Comp. Ex.	Ex. 24	Ex. 25
	C16	C17	C18	(Comparative	(D-75
	(D-75 with	(D-75 with	(D-75	Ex. C17	w/2.78%
	additional	additional 1.25%	w/1.25%	w/0.70%	CRIMSON
	1.25%	STD and Increased	PMT1 and	CRIMSON &	and Incr.
	STD)	Viscosity)	Incr. Viscosity)	Incr. Viscosity	Viscosity)
Viscosity (cps)	1667	2660	2660	2667	2883
LIGHT TRANSMISSION OF THROUGH THE WET FILM (Y)
Film Thickness/gpc
0.022 in./1.37	73	71	72	65	58
0.032 in./2.0	69	68	65	58	50
0.064 in./4.0	44	47	42	30	22
RED COLOR INTENSITY (a) OF THE WET FILM
Film Thickness/gpc
0.022 in./1.37	3	3	3	8	12
0.032 in./2.0	5	5	6	11	18
0.064 in./4.0	16	14	14	26	40
RELATIVE DARKNESS OF THE WET FILM
BLACK/DARK = 0 and white/light = 100)
Film Thickness gpc
0.022 in./1.37	88	87	88	85	81
0.032 in./2.0	86	86	85	81	76
0.064 in./4.0	72	74	71	61	54
YELLOW COLOR INTENSITY (b) OF THE WET FILM
Film Thickness gpc
0.022 in./1.37	4	3	2	3	0
0.032 in./2.0	5	4	2	4	0
0.064 in./4.0	11	9	5	10	8

TABLE 17
IMPACT OF DRYING ON LIGHT AND
COLOR TRANSMISSION THROUGH FILMS
		Comp. Ex. C17		Ex. 24	Ex. 25
	Comp. Ex. C16	(D-75 with additional	Comp. Ex. C18	(Comparative Ex. C17	(D-75 w/2.78%
	(D-75 with additional	1.25% STD and Increased	(D-75 w/1.25% PMT1	w/0.70% CRIMSON &	CRIMSON and Incr.
	1.25% STD)	Viscosity)	and Incr. Viscosity)	Incr. Viscosity	Viscosity)
Viscosity (cps)	1667	2660	2660	2667	2883
Δ LIGHT TRANSMISSION DURING DRYING (ΔY)
Film Thickness/gpc
0.022 in./1.37	73 to 47	71 to 46	72 to 47	65 to 43	58 to 39
0.032 in./2.0	69 to 43	68 to 37	65 to 40	58 to 36	50 to 32
0.064 in./4.0	44 to 56	47 to 33	42 to 32	30 to 23	22 to 21
0.128 in/8.0	too fluid	NA to 22	NA to 19	NA to 17	NA to 17
Δ RED INTENSITY (higher values indicate a more intense red)
Film Thickness/gpc
0.022 in./1.37	3 to 6	3 to 6	3 to 6	8 to 11	12 to 16
0.032 in./2.0	5 to 9	5 to 10	6 to 10	11 to 16	18 to 22
0.064 in./4.0	16 to 13	14 to 18	14 to 20	26 to 28	40 to 35
Δ DARKNESS OF THE FILM (where black = 0 and white = 100)
Film Thickness gpc
0.022 in./1.37	88 to 74	88 to 74	88 to 74	85 to 71	81 to 69
0.032 in./2.0	86 to 72	86 to 68	85 to 69	81 to 67	76 to 63
0.064 in./4.0	72 to 72	74 to 64	71 to 63	61 to 55	54 to 53
Δ YELLOW COLOR INTENSITY (higher values indicate a more intense yellow color)
Film Thickness gpc
0.022 in./1.37	4 to 9	3 to 9	2 to 6	3 to 8	0 to 5
0.032 in./2.0	5 to 11	4 to 12	2 to 8	4 to 11	0 to 7
0.064 in./4.0	11 to 12	9 to 12	5 to 10	10 to 16	8 to 11

TABLE 18A
COLOR AND FADING CHARACTERISTICS OF 0.022″ (0.056 CM)
THICK FUGITIVE COLOR FILMS FOLLOWING EXPOSURE
TO SUNLIGHT
		Comp. Ex.		Ex. 24
		C17 (D-75		(Compara-	Ex. 25
	Comp. Ex.	with	Comp. Ex.	tive Ex.	(D-75
	C16 (D-75	additional	C18 (D-75	C17	w/2.78%
	with	1.25%	w/1.25%	w/0.70%	CRIM-
	additional	STD and	PMT1 and	CRIMSON	SON and
	1.25%	Increased	Incr.	& Incr.	Incr.
	STD)	Viscosity)	Viscosity)	Viscosity	Viscosity)
Viscosity	1667	2660	2660	2667	2883
(cps)
A. Lightness of the Color (L value where black = 0 and white = 100)
initial	49	51	50	49	48
after 6 K	48	47	46	46	45
Langleys
after 12 K	48	48	47	47	47
Langleys
after 18 K	47	47	46	46	46
Langleys
after 24 K	46	46	46	45	44
Langleys
after 30 K	44	44	43	43	44
Langleys
B. Red Intensity (positive (a) values indicate intensity of red;
negative values indicate green color)
initial	9	10	11	19	24
after 6 K	−2	−1	7	1	7
Langleys
after 12 K	−2	−1	5	0	2
Langleys
after 18 K	−2	−2	3	−2	−1
Langleys
after 24 K	−2	−2	2	−1	−2
Langleys
after 30 K	−3	−2	1	−2	−2
Langleys
C. Yellow Color Intensity (positive (b) values indicates yellow,
negative values indicate blue)
initial	5	6	3	8	5
after 6 K	5	4	4	5	4
Langleys
after 12 K	6	6	6	6	5
Langleys
after 18 K	7	7	6	7	5
Langleys
after 24 K	7	7	6	7	5
Langleys
after 30 K	7	7	7	7	6
Langleys

TABLE 18B
COLOR AND FADING CHARACTERISTICS OF 0.032″ (0.081 CM)
THICK FUGITIVE COLOR FILMS FOLLOWING EXPOSURE
TO SUNLIGHT
		Comp. Ex.		Ex. 24
		C17 (D-75		(Compara-	Ex. 25
	Comp. Ex.	with	Comp. Ex.	tive Ex.	(D-75
	C16 (D-75	additional	C18 (D-75	C17	w/2.78%
	with	1.25%	w/1.25%	w/0.70%	CRIM-
	additional	STD and	PMT1 and	CRIMSON	SON and
	1.25%	Increased	Incr.	& Incr.	Incr.
	STD)	Viscosity)	Viscosity)	Viscosity	Viscosity)
Viscosity	1667	2660	2660	2667	2883
(cps)
A. Lightness of the Color (L value where black = 0 and white = 100)
initial	52	53	52	50	48
after 6 K	49	54	55	55	47
Langleys
after 12 K	50	53	55	55	49
Langleys
after 18 K	49	54	56	55	49
Langleys
after 24 K	48	52	54	54	47
Langleys
after 30 K	46	50	52	52	45
Langleys
B. Red Intensity (positive (a) values indicate intensity of red;
negative values indicate green color)
initial	16	15	19	26	31
after 6 K	0	1	9	4	10
Langleys
after 12 K	0	0	7	2	5
Langleys
after 18 K	−1	−1	6	0	2
Langleys
after 24 K	−1	0	4	0	0
Langleys
after 30 K	−1	−1	4	0	−1
Langleys
C. Yellow Color Intensity (positive (b) values indicates yellow,
negative values indicate blue)
initial	9	9	6	12	9
after 6 K	6	6	5	7	6
Langleys
after 12 K	8	8	7	8	7
Langleys
after 18 K	9	9	7	9	7
Langleys
after 24 K	9	10	8	10	7
Langleys
after 30 K	9	10	9	10	7
Langleys

TABLE 18C
COLOR AND FADING CHARACTERISTICS OF 0.064″ (0.163 CM)
THICK FUGITIVE COLOR FILMS FOLLOWING EXPOSURE
TO SUNLIGHT
		Comp. Ex.		Ex. 24
		C17 (D-75		(Compara-	Ex. 25
	Comp. Ex.	with	Comp. Ex.	tive Ex.	(D-75
	C16 (D-75	additional	C18 (D-75	C17	w/2.78%
	with	1.25%	w/1.25%	w/0.70%	CRIM-
	additional	STD and	PMT1 and	CRIMSON	SON and
	1.25%	Increased	Incr.	& Incr.	Incr.
	STD)	Viscosity)	Viscosity)	Viscosity	Viscosity)
Viscosity	1667	2660	2660	2667	2883
(cps)
A. Lightness of the Color (L value where black = 0 and white = 100)
initial	52	54	53	52	51
after 6 K	60	61	59	61	58
Langleys
after 12 K	60	60	60	61	59
Langleys
after 18 K	60	60	60	60	59
Langleys
after 24 K	59	59	59	59	58
Langleys
after 30 K	57	58	58	58	57
Langleys
B. Red Intensity (positive (a) values indicate intensity of red;
negative values indicate green color)
initial	21	27	29	35	46
after 6 K	2	4	11	8	15
Langleys
after 12 K	1	3	9	5	10
Langleys
after 18 K	0	1	7	2	6
Langleys
after 24 K	0	2	6	2	5
Langleys
after 30 K	0	2	5	2	4
Langleys
C. Yellow Color Intensity (positive (b) values indicates yellow,
negative values indicate blue)
initial	13	17	12	17	18
after 6 K	9	9	6	8	7
Langleys
after 12 K	10	11	7	9	7
Langleys
after 18 K	11	11	8	10	8
Langleys
after 24 K	12	13	9	11	9
Langleys
after 30 K	13	13	10	12	9
Langleys

TABLE 18D
COLOR AND FADING CHARACTERISTICS OF 0.128″ (0.325 CM)
THICK FUGITIVE COLOR FILMS FOLLOWING EXPOSURE
TO SUNLIGHT
		Comp. Ex.		Ex. 24
		C17 (D-75		(Compara-	Ex. 25
	Comp. Ex.	with	Comp. Ex.	tive Ex.	(D-75
	C16 (D-75	additional	C18 (D-75	C17	w/2.78%
	with	1.25%	w/1.25%	w/0.70%	CRIM-
	additional	STD and	PMT1 and	CRIMSON	SON and
	1.25%	Increased	Incr.	& Incr.	Incr.
	STD)	Viscosity)	Viscosity)	Viscosity	Viscosity)
Viscosity	1667	2660	2660	2667	2883
(cps)
A. Lightness of the Color (L value where black = 0 and white = 100)
initial	43	45	41	43	43
after 6 K	62	61	58	63	56
Langleys
after 12 K	61	60	57	62	56
Langleys
after 18 K	62	60	57	62	57
Langleys
after 24 K	61	58	56	61	56
Langleys
after 30 K	59	59	58	62	57
Langleys
B. Red Intensity (positive (a) value indicate intensity of red;
negative values indicate green color)
initial	20	33	31	38	46
after 6 K	5	10	17	15	24
Langleys
after 12 K	3	6	14	10	19
Langleys
after 18 K	1	4	11	7	12
Langleys
after 24 K	2	4	11	6	11
Langleys
after 30 K	2	3	8	5	8
Langleys
C. Yellow Color Intensity (positive (b) values indicates yellow,
negative values indicate blue)
initial	11	22	13	20	24
after 6 K	9	11	8	12	16
Langleys
after 12 K	12	13	9	13	15
Langleys
after 18 K	12	14	9	14	16
Langleys
after 24 K	13	15	10	15	15
Langleys
after 30 K	13	13	9	13	16
Langleys

As described above, the data show that the hiding ability of the films increased (percent light transmission decreased) with film thickness (coverage level). The CRIMSON pigmented Example 25 was significantly superior to the other formulations. Example 24, the standard D-75, with additional 1.25% STD, enhanced with a small amount of CRIMSON, was better than the other formulations, Comparative Examples C16-C18. Further, while iron oxide provided greater film opacification, CRIMSON was superior in terms of color intensity. Example 24 was equivalent to iron oxide in that regard while Example 25 provided a considerably brighter color.

The data also showed that color fading (fire retardant disappearance) slowed with increasing fire retardant solution coverage level. The exposed color values in Tables 18A-D show that the 0.032 inch (0.056 cm) thick Comparative Example C16 films of standard D-75 lost its red color within about 3,000 Langleys (1.26×10 8 J/M 2 ) of exposure. The exposure required to bleach the Comparative Example C16 films increased to more than 6,000 Langleys (2.51×10 8 J/M 2 ) for 0.064 inch (0.163 cm, 4 gpc or 1.4 L/M 2 ) films and to more than 12,000 Langleys (5.02×10 8 J/M 2 ) for 0.128 inch (0.325 cm, 8 gpc or 2.8 L/M 2 ) films.

CRIMSON fugitive pigment dispersion was used to colorize PHOS-CHEK® D-75 fire retardant solution in Example 25. The data show that when exposed in accordance with U.S. -Forest Service protocols—0.022 inch (0.056 cm) films and 18,000 Langleys (7.53×10 8 J/M 2 ) of natural sunlight exposure—the solution totally disappeared. Accordingly, the requirements of the U.S. Forest Service specifications for color fade were met by the 0.022 inch (0.056 cm) films of Example 25. When the experiment was performed on 0.032 inch films, although some color did remain, the color also faded to an acceptable level.

When applied at a 0.064 inch thickness, however, the Example 25 films retained a small amount of red color after even 30,000 Langleys (12.55×10 8 J/M 2 ) of sunlight exposure. Further, when applied at 0.128 inch thickness (8 gpc or 2.8 L/M 2 ) the CRIMSON colorized film retained a greater red color intensity after 24,000 Langleys (10.04×10 8 J/M 2 ) of sunlight exposure than Comparative Example C16—the standard PHOS-CHEK® D-75, with additional 1.25% STD—possessed prior to exposure.

Examples 26-32, Comparative Examples C19, C29, OpC16, and OpC17—Comparison of Unopacified Fire Retardants

Samples of PHOS-CHEK® D-75 (uncolored) and D-75 colored with added STD (the standard fugitive powder pigment) dry-powder fire retardants were prepared similarly as for the Comparative Examples previously described above.

The dry powders were mixed with water to the standard use-level in the standard manner, i.e., at a mix ratio of 143.8 grams per liter of tap water (1.2 pounds per gallon) to form mother solutions. 1.8 liters of each mother solution was prepared. The viscosity of each mother solution was 1500±50 cps when measured at about 70° F. (21° C.)

These uncolored and STD colored mother solutions were then divided into 400 milliliter aliquots. Comparative Examples C19 and C20, respectively, are the uncolored and STD colorized mother solutions from which the Examples 26-29 and 30-32, respectively, were prepared. Examples 26-29 were formed by adding the fugitive-color aqueous pigment colorant suspension, SG517-31 (“APD1”) manufactured by Day-Glo Color Corp., to the uncolored mother solutions. Examples 30-32 were formed by adding APD1 to the STD-colored mother solutions. Comparative Examples OpC16 and OpC17 were colorized with 1.0% and 1.25% red iron oxide respectively. The preparation of these solutions is summarized below:

	Colorant
	Sample Number	STD	APD1	Opacified
	Comp. Ex. C19	NO	NO	NO
	26	NO	YES	NO
	27	NO	YES	NO
	28	NO	YES	NO
	29	NO	YES	NO
	Comp. Ex. C20	YES	NO	NO
	30	YES	YES	NO
	31	YES	YES	NO
	32	YES	YES	NO
	Comp. Ex. OpC16	NO	NO	YES
	Comp. Ex. OpC17	NO	NO	YES

Each addition of the aqueous pigment dispersion APD1 was made with sufficient agitation to uniformly distribute the dispersion into the mother solution aliquot within 5 minutes. The APD1 fugitive color pigment suspension was similar to CRIMSON, except a different dye was incorporated in the polymer particle. The amount of pigment solids and suspension added to the aliquots is described below in Table 20.

Opacified Comparative Examples OpC16 and OPC17 contained red iron oxide as the color pigment and were prepared for comparative purposes. Comparative Example OpC16 was the PHOS-CHEK® D-75 fire retardant with 0.126% red iron oxide pigment in the solution (1.0% red iron oxide in the powder). This iron oxide colored product is commercially available and has been used in the field with adequate visibility. Comparative Example OpC17 was D-75 with the amount of added red iron oxide pigment increased to 0.157% based on solution weight.

Films of the various formulations were prepared on glass plates as described previously above. In this case, three different film thicknesses of each formulation were prepared: 0.022, 0.032, and 0.064 inches (0.559, 0.813, and 1.626 mm). These thicknesses are equivalent to a wet application rate of 1.5, 2.0 and 4.0 gallons of fire retardant solution per 100 square feet of surface (gpc). Fugitive color fading was evaluated in accordance with U.S. Forest Service requirements on films with a thickness of 0.022″ (0.559 mm). As described earlier, a 2.0 gpc (0.032″, 0.813 mm) fire retardant coverage level is considered adequate for the “average” fire in many fuel types while a 4.0 gpc (0.064″, 0.626 mm) fire retardant application rate is the minimum requirement for heavy brush and timber where fugitive colored fire retardants are more difficult to see. It is, therefore, likely that the 4.0 gpc or 0.064″ (1.626 mm) situation would more nearly approximate a problem field condition.

TABLE 20
Composition of Solutions from the Mother Solutions.
			% APD1
		Added APD1	Color	%
Sample	Mother	Color Suspen-	Suspen-	Pigment	Pigment
No.	Solution	sion (g)	sion**	Solids*	Level&Circlesolid;
26	Uncolored	0.708	0.18	0.078	0.50
27	Uncolored	1.044	0.26	0.115	0.73
28	Uncolored	1.396	0.35	0.154	0.98
29	Uncolored	1.753	0.44	0.193	1.23
C19	Uncolored	0	0	0	0
C20	STD	0	0	0	0
30	STD	0.348	0.09	0.0328	0.24
31	STD	0.704	0.18	0.077	0.49
32	STD	1.057	0.26	0.116	0.74
Comp. Ex.	Fe 2 O 3	0	0	0	0
OpC16
Comp. Ex.	Fe 2 O 3	0	0	0	0
OpC16
*APD1 color suspension contained about 44% pigment solids.
**In fire retardant solution when mixed at use-level, does not include the STD pigment in the D-75-with-STD mother solutions.
&Circlesolid;Relative to Standard PHOS-CHEK ® D-75 with STD added which contained 0.157% pigment solids. Does not include the STD pigment in the D-75-with-STD mother solution.

The films were characterized using the same procedures as described previously above. Light transmission measurements through the wet and dry films were obtained 20 minutes, 120 minutes, and about 24 hours after application. The plates were stored at ambient temperatures (70±5° F., 21° C.±3° C.) during that time. After 20 minutes, the film was still wet at the time of measurement and some flow occurred when the film was held in a vertical position. After 2 hours, the film was still somewhat wet but flow did not occur when the film was held in a vertical position. The film was totally dry 24 hours after application. These time periods and degrees of dryness encompassed that time and condition, in practice, when the visibility of the fire retardant application is needed and desired. The transmission values were converted to opacification values, i.e., opacification is equal to 100 minus transmission. Table 21 below illustrates the degree of opacity exhibited by the thus formed films.

Color intensity was measured on all films after exposure to 0, 6K, 12K and 18K Langleys (0, 2.51, 5.02, and 7.53×10 8 J/M 2 ) of natural sunlight. In those cases where traces of a red color continued to be present in the films after 18K Langleys (7.53×10 8 J/M 2 ), exposure of the films was continued to 24K Langleys (10.04×10 8 J/M 2 ). Table 22 below illustrates the color intensity of the fresh dried (un-exposed) films. Tables 23, 24, and 25 below illustrate the rate of fading (fugitive) as a function of sunlight exposure.

TABLE 21
THE IMPACT OF PIGMENT CONCENTRATION AND FILM THICKNESS ON OPACIFICATION
	22 milliinch Film Thickness	32 milliinch Film Thickness	64 milliinch Film Thickness
Sample	Opacification (100-Y)	Opacification (100-Y)	Opacification (100-Y)
Number	20 min.⋄	2 hrs.⋄	24 hrs.⋄	20 min.	2 hrs.	24 hrs.	20 min.	2 hrs.	24 hrs.
C19	14	14	45	14	15	41	16	15	45
26	29	29	56	33	35	55	53	43	65
27	34	34	64	39	39	65	60	52	66
28	39	39	62	46	48	69	67	59	69
29	43	43	62	52	53	68	72	67	76
C20	29	28	55	35	35	62	47	47	63
30	36	34	59	40	41	65	63	58	70
31	42	41	65	48	48	67	71	60	74
32	45	45	66	54	55	74	74	67	78
Comp. Ex.	—	60	77	69	73	85	—	91	92
Op16
Comp. Ex.	—	68	83	87	74	87	—	91	93
Op17
⋄Indicates length of time between film drawdown and measurement. 20 minutes is considered equal to wet; 24 hrs. is considered equal to dry.

The data in Table 21 show that opacity increased with (i) film thickness, (ii) the amount of pigment in the formulation and (iii) the degree of dryness of the application. The impact of 2 hours drying of the fire retardant solution at the ambient indoor temperatures in this study was relatively insignificant in terms of the films' abilities to hide that on which they were applied. However, the fire retardant salts and other water soluble components in the fire retardant formulation precipitate during drying and would be expected to contribute to film opacification. Such precipitation would occur more rapidly during actual fire use when temperatures are higher and drying winds present. Accordingly, two hours in actual fire use conditions would likely contribute more opacity than that opacity generated from these relatively mild ambient indoor conditions.

Comparison of the data for the samples that were made at equal pigment loadings show that the aqueous pigment suspension APD1 was superior in opacification ability to the currently used dry-powder STD pigment. Example 28 had a 0.154% pigment loading of APD1, while Comparative Example C20 had a 0.157% pigment loading of STD dry-powder pigment. Nevertheless, Example 28 was superior to Comparative Example C20 in opacity. Similarly, Example 29 had a 0.193% pigment loading of APDl, while Example 30 had a 0.038% loading of APD1 and 0.157% loading of STD for a total of 0.195% pigment loading, but Example 29 was superior to Example 30 in opacity.

Non-fugitive red iron oxide was superior to both the dry-powder STD and the aqueous pigment dispersion APD1 in opacifying capability. The data show that iron oxide levels in excess of the currently used level do not appreciably increase opacity.

TABLE 22
THE COLOR INTENSITY OF NON-FADED,
DRY FUGITIVE COLOR FILMS OF VARYING THICKNESS
	22 milliinch	32 milliinch	64 milliinch
	Film Thickness	Film Thickness	Film Thickness
Sample	Reflectance	Reflectance	Reflectance
Number	L	a	b	L	a	b	L	a	b
C19	56	−5	2	56	−5	3	57	−6	4
26	49	14	−1	52	21	1	49	21	1
27	47	19	−1	47	23	1	48	28	2
28	46	22	0	49	30	2	46	33	4
29	46	27	1	46	32	3	48	39	5
C20	50	10	7	49	14	10	48	17	12
30	48	17	7	48	22	9	47	26	11
31	47	23	7	49	29	9	46	30	11
32	46	26	7	47	33	10	46	38	13
Comp. Ex.	45	22	16	43	24	17	42	27	18
Op16
Comp. Ex.	43	25	18	43	27	19	40	28	19
Op17

The data in Table 22 reveal that the intensity of the red color component (a Value) in the fire retardant film increased with pigment content and film thickness. The data is in accordance with the observation that fire retardant films, in general, become darker and more intensely red with increasing pigment content of the formulation.

Similar to above, comparison of the data for the samples that were made at equal pigment loadings show that the aqueous pigment suspension APD1 provided a considerably more intense red color than the currently used dry-powder STD pigment. Example 28 had a 0.154% pigment loading of APD1, while Comparative Example C20 had a 0.157% pigment loading of STD dry-powder pigment. Yet Example 28 was superior to Comparative Example C20 in color. Similarly, Example 29 had a 0.193% pigment loading of APD1, while Example 30 had a 0.038% loading of APD1 and 0.157% loading of STD for a total of 0.195% pigment loading. Yet Example 29 was superior to Example 30 in color.

The D-75 formulations provided red intensity values equal to 0.126% red iron oxide when the D-75 formulations contained about 0.115% of the APD1 pigment suspension or a combination of 0.157% of the currently used STD dry-pigment and 0.038% of the APD1 pigment suspension. The data indicate that red intensity increased more with pigment loading when using the fugitive pigments than when using red iron oxide. In the latter case it may be due to the loading of iron oxide having reached a point of diminishing return. Therefore, the visibility of the fugitive films would improve to a greater extent than would the visibility of the iron oxide pigment films as the fire retardant application rate increases.

The data show that film darkened (decreased L Value) with increased pigment loading regardless of the type of pigment. Increased film thickness, on the other hand, appeared to have little effect on the L Value.

TABLE 23
THE COLOR INTENSITY OF FADED FUGITIVE COLOR
FILMS OF VARYING THICKNESS AFTER 6K LANGLEYS
(2.51 × 10 8 J/M 2 ) EXPOSURE
	22 milliinch	32 milliinch	64 milliinch
	Film Thickness	Film Thickness	Film Thickness
Sample	Reflectance	Reflectance	Reflectance
Number	L	a	b	L	a	b	L	a	b
C19	57	−2	2	58	−1	4	59	−6	4
26	56	7	3	60	11	6	58	12	6
27	55	10	4	56	13	6	58	17	8
28	53	12	4	58	19	7	56	22	9
29	54	16	5	56	21	7	59	28	11
C20	58	−2	4	59	0	7	59	1	9
30	57	3	4	58	5	6	58	8	8
31	56	8	5	59	11	7	57	13	9
32	56	11	5	58	16	8	57	21	11

TABLE 24
THE COLOR INTENSITY OF FADED FUGITIVE COLOR
FILMS OF VARYING THICKNESS AFTER 12K LANGLEYS
(5.02 × 10 8 J/M 2 ) EXPOSURE
	22 milliinch	32 milliinch	64 milliinch
	Film Thickness	Film Thickness	Film Thickness
Sample	Reflectance	Reflectance	Reflectance
Number	L	a	b	L	a	b	L	a	b
C19	55	0	7	57	−5	3	58	2	10
26	53	2	3	57	6	9	58	7	10
27	54	4	7	57	7	9	58	9	10
28	51	3	5	53	8	8	57	12	11
29	49	4	5	53	9	8	56	16	12
C20	56	0	8	58	2	11	58	2	10
30	55	2	9	58	4	11	60	4	12
31	52	3	8	56	6	11	59	6	13
32	55	5	9	56	8	12	59	8	12

TABLE 25
THE COLOR INTENSITY OF FADED FUGITIVE
COLOR FILMS OF VARYING THICKNESS AFTER
18K (7.53 × 10 8 J/M 2 ) LANGLEYS EXPOSURE
	22 milliinch	32 milliinch	64 milliinch
	Film Thickness	Film Thickness	Film Thickness
Sample	Reflectance	Reflectance	Reflectance
Number	L	a	b	L	a	b	L	a	b
C19	48	−3	4	52	−2	6	51	−2	6
26	51	−2	3	55	0	6	53	1	7
27	52	−1	3	55	0	5	53	2	7
28	51	−1	3	53	1	5	54	3	7
29	51	0	3	54	2	5	53	5	8
C20	49	−3	6	56	−1	10	57	0	10
30	52	−2	6	54	−1	8	56	2	12
31	53	−1	6	57	0	8	55	2	10
32	55	0	6	59	3	9	56	5	11

Comparison of the data in Table 22 with that in Tables 23, 24, and 25 illustrates the change in the color characteristics (L, a and b values) of the dried fire retardant films as a function of sunlight exposure, i.e., after 0, 6K, 12K and 18K Langleys (0, 2.51, 5.02, and 7.53×10 8 J/M 2 ) of outdoor Arizona sunlight radiation. The red iron oxide pigmented films were not subjected to sunlight exposure since they do not fade.

The data reveal that the rate of color disappearance from both the dry-powder STD and the aqueous-pigment-dispersion colorized fire retardant films decreased with the concentration of pigment in the film and the thickness of the fire retardant film. Measurements made on equivalent films show that the rate of fade of the pigment of the aqueous-pigment-dispersion of this invention was significantly slower than the dry-powder pigment.

Even the thickest 64 milliinch (1.626 mm) film containing the conventionally used STD dry-powder fugitive pigment lost all of its red color component in less than 6K Langleys (2.51×10 8 J/M 2 ) of sunlight exposure, i.e., in less than 10 days in the October sun near Phoenix, Ariz. The pigment APD1 suspended in the aqueous-pigment-dispersion met the U.S. Forest Service fading requirement of the total disappearance of color in a 22 milliinch (0.559 mm) film after 18K Langleys exposure (7.53×10 8 J/M 2 ), at all the pigment loading levels in the Examples, while retaining more red color component after 6K Langleys (2.51×10 8 J/M 2 ) of sunlight exposure than were contained in the dry-powder pigment STD containing fire retardants prior to exposure.

Most of the red color component in thin films (22 milliinch or 0.559 mm) of the pigment APD1 suspended in the aqueous-pigment-dispersion faded after 12K Langleys (5.02 ×10 8 J/M 2 ) of exposure (in 32 days), however some red color remained even after 18K Langleys (7.53×10 8 J/M 2 ) (in 53 days) in the thicker (64 milliinch or 1.626 mm) films. The last traces of red color component in even the thickest of the films disappeared between 18K and 24K Langleys (7.53 and 10.04 ×10 8 J/M 2 ) of sunlight exposure.

The data shows that the suspended pigment APD1 in the aqueous-pigment-dispersion was superior to the dry-powder pigment STD in terms of its ability to opacify the base D-75 fire retardant. However, neither of the fugitive color pigments by itself was equivalent to red iron oxide with respect to opacification or hiding ability. Therefore, for applications where opacification or hiding ability is particularly important, a hiding pigment such as, for example, titanium dioxide can be included to improve the opacification or hiding ability of the fire retardants.

Examples 33-57, Comparative Examples C21-C35 and OpC18-OpC20—Color, Visibility, Stability, Corrosivity, and Pumpability

In the previous examples, the aqueous pigment dispersions of this invention were added to fire retardant solutions prepared by mixing dry-powder concentrates in water at their prescribed mix ratios. As described previously, other types of wildland fire retardant concentrates are also known.

The aqueous pigment dispersions of this invention were added to all three of the fire retardant concentrates described previously—dry powder concentrates, fluid concentrates, and liquid concentrates—and to their solutions prepared at their product-specific mix ratios. This study was conducted to determine if the point of introduction of the aqueous pigment dispersion into the fire retardant mixture has any impact on its ability both to colorize and then to fade after exposure to natural sunlight.

Seven fire retardant concentrates were prepared: i) an uncolored dry-powder type—PHOS-CHEK® D-75, ii) a colored dry-powder type—D-75 containing STD dry-powder pigment, iii) an uncolored fluid concentrate type prepared from the same components as PHOS-CHEK® D-75, iv) an uncolored liquid concentrate type fire retardant prepared with a 10-34-0 liquid fertilizer solution, v) an uncolored fluid concentrate type prepared with the same components as PHOS-CHEK® ARL/AFL fire retardants, vi) D-75 containing 1.0% TiO 2 and 0.25% red iron oxide, and vii) the uncolored fluid concentrate of (iii) containing 0.49% TiO 2 and 0.12% red iron oxide.

Concentrates (i), (ii) and (vi) were dry-powder types where the constituent ingredients were mixed together without adding water. These dry-powder products were subsequently mixed with water at their prescribed mix ratios to form the fire retardant solutions ready for application. Concentrates (iii), (iv), (v) and (vii) were fluid concentrate types. These fluids were mixed with water at their product-specific mix ratios to form the fire retardant solutions ready for application. Only concentrate (ii) contained a colorizing pigment.

The effect of the addition of the aqueous pigment dispersions of this invention was tested by adding an aqueous pigment dispersion (either CRIMSON or APD1) to aliquots of each of the concentrates and to each of the fire retardant solutions prepared from each concentrate. For comparison, the currently used STD dry-powder fugitive pigment was also added to aliquots of each of the concentrates and also to each of the solutions prepared therefrom.

The appearance of each of the mixtures of the concentrates and the colorants was noted and then the concentrates were mixed with water at their product- specific ratio to form the end-use fire retardant solution. This procedure resulted in solutions of each of the fire retardant types prepared (i) with the color pigment added to the concentrate-prior to the preparation of the end-use fire retardant solution, and (ii) with the addition occurring after the preparation of the end-use solution.

Films 32 milliinch (0.813 mm) thick were prepared on glass plates from each of the diluted solutions. The visual appearance of the films was noted and the degree of opacification, color, color intensity and rate of fade after exposure to natural sunlight was determined photometrically. The presence/absence of pigments and opacifiers, and the point of mixing when the pigments/opacifiers were added, for each test sample are summarized below:

		Opaci-	Pigments/Opacifiers
Ex. No.	Pigment Type	fied	Added To
33, 34	Aqueous Dispersion	NO	Dry-Powder Concentrate
35	Aqueous Dispersion	YES	Dry-Powder Concentrate
36, 37	Dry-Powder and	YES	Dry-Powder Concentrate
	Aqueous Dispersion
38, 39	Dry-Powder and	NO	Fluid Concentrate
	Aqueous Dispersion
43, 44	Aqueous Dispersion	NO	Fluid Concentrate
40	Aqueous Dispersion	YES	Fluid Concentrate
41, 42	Aqueous Dispersion	NO	Liquid Concentrate
45-47, 51,	Aqueous Dispersion	NO	Added At Final Dilution
52, 54-57
48, 53	Aqueous Dispersion	YES	Added At Final Dilution
49, 50	Dry-Powder and	YES	Added At Final Dilution
	Aqueous Dispersion
Comparative Examples
C21, C23, C25,	None	NO	No Additional Pigments/
C27			Opacifiers Added
C22, C30, C31	Dry-Powder	NO	Dry-Powder Concentrate
C24, C26, C28	Dry-Powder	NO	Fluid Concentrate
C32-C35	Dry-Powder	NO	Added At Final Dilution
OpC18	None	YES	Dry-Powder Concentrate
OpC19	Dry-Powder	YES	Dry-Powder Concentrate
OpC20	None	YES	Fluid Concentrate

As described above, the concentrates and solutions, were mixed with either the standard dry-powder fugitive color pigment (STD) or with one of the aqueous pigment suspension colorants obtained from Day-Glo Color Corporation (CRIMSON or APD1). In these tests, the CRIMSON and APD1 are considered equivalent in being both aqueous pigment suspensions. The colorants and/or opacifiers were added to either the concentrate prior to dilution to final end-use fire retardant form, or added to the end-use solution as indicated in the table above.

Examples 33-37 were prepared by adding the aqueous pigment suspension colorant to the dry powder D-75 concentrate. Examples 35-37 also included opacifiers. Examples 36 and 37 further included the STD dry-pigment.

Examples 38-40, 43 and 44 were prepared by adding the aqueous pigment suspension colorant to the fluid concentrate type fire retardants prior to mixing with water. Examples 38, and 39 also included STD dry-powder pigment. Example 40 included opacifiers.

Examples 41 and 42 were prepared by adding the aqueous pigment suspension colorant to the liquid concentrate type fire retardant prior to mixing with water.

Comparative Example C22 added the STD dry-pigment to the D-75 dry-powder concentrate type fire retardant prior to mixing with water.

Comparative Examples C24, C26, and C28 added the STD dry-pigment to the fluid concentrate type fire retardant prior to mixing with water.

Opacified Comparative Example OpC19 added the STD dry-pigment and opacifiers to the dry-powder concentrate type fire retardant prior to mixing with water.

Opacified Comparative Example OpC20 added just the opacifiers to a fluid concentrate type fire retardant prior to mixing with water, while Opacified Comparative Example OpC18 added just the opacifiers to the dry-powder concentrate type fire retardant prior to mixing with water, each without any fugitive colorants.

As described above, after addition of the pigments and/or opacifiers, each of the above concentrates were diluted to their end-use concentration.

Comparative Examples C21, C23, C25, and C27 were unmodified base fire retardants. Comparative Examples C22, C30, and C31 were PHOS-CHEK® D-75 dry powder formulation that included the STD dry-powder pigment.

Examples 45-57 added the aqueous pigment dispersion to the final fire retardant after dilution to the end use concentration. Examples 48 and 53 also included opacifiers. Examples 49 and 50 included opacifiers and the STD dry-powder pigment. Similarly, Comparative Examples C32-C35 added the dry-powder pigment to the final fire retardant after dilution to the end-use concentration.

Further dilution was not necessary, of course, in the above cases where the colorant was added to the final fire retardant solution. Each of the solutions was allowed to set undisturbed overnight so that any entrapped air would dissipate. Films of each of the solutions were then drawn down on glass plates in the normal manner to a thickness of 32 milliinch (0.813 mm). The visual appearance of the film, wet and dry opacification, initial color and color intensity were measured within about 24 hours of film preparation. In some cases, the color and appearance of the films were visually non-uniform. In those cases, instrumental measurement of opacity and color intensity was not meaningful. Consequently, instrumental measurements were not made in those cases. Instead, the appearance of the film was noted.

After the twenty four hour data were obtained, the glass plates were exposed to natural sunlight in the Phoenix, Ariz. area. The remaining (faded) color and color intensity of the films were measured after 6K, 12K, 18K (2.51, 5.02, and 7.53 ×10 8 J/M 2 ) and, in some cases, 24K Langleys (10.04×10 8 J/M 2 ) of natural sunlight exposure. The data are shown in Tables 26A and 26B below. Table 26A shows the data when the pigment was added to the fire retardant concentrate prior to the concentrate's dilution to the final end-use concentration. Table 26B shows the data obtained when the pigment was added to the fire retardant fluid at its end-use concentration.

In Tables 26A and 26B, the pigment addition percentage does not include any pigment in the base material. The CRIMSON and APD1 aqueous pigment dispersions contained 44% active pigment solids. The STD dry-pigment contained 100% active pigment solids.

TABLE 26A
The Impact Of The Timing Of Pigment Addition On The Opacity And Color Of
32 Milliinch Thick Fire Retardant Films (All measurements were made on diluted
solutions. All measurements, except opacification at 2 hours, were made on dry films.)
	%	Color Characterization
			Opacification	0 Langley	6K Langley	12K Langley	18K Langley
Sample		Pigment Addition	(100-Y)	Exposure	Exposure	Exposure	Exposure
Number	Base Material	Type	(%)	2 hrs	24 hrs.	L	a	b	L	a	b	L	a	b	L	a	b
C21	D-75 powder	none	0.000	14	41	56	−5	3	62	−3	3	60	−2	6	53	−3	4
33	D-75 powder	CRIMSON	0.157	Pigment suspension agglomerated when added to dry powder: meaningful
				opacification and color measurements could not be obtained.
34	D-75 powder	APD1	0.157	Pigment suspension agglomerated when added to dry powder: meaningful
				opacification and color measurements could not be obtained.
C22	D-75 powder	STD	0.157	35	59	50	15	11	61	−1	6	58	2	11	55	−2	9
OpC18	OpD-75 powder	none	0.000	65	73	61	7	8	61	9	9	60	11	11	61	9	10
35	OpD-75 powder	CRIMSON	0.157	58	71	55	15	9	57	14	11	57	14	12	57	12	11
36	C22 powder	CRIMSON	0.0785	Pigment suspension agglomerated when added to dry powder: meaningful
	opacified			opacification and color measurements could not be obtained.
37	C22 powder	APD1	0.0785	Pigment suspension agglomerated when added to dry powder: meaningful
	opacified			opacification and color measurements could not be obtained.
OpC19	C22 powder	STD	0.0785	42	64	49	22	15	60	1	8	59	2	12	56	−1	11
	opacified
C23	HVW conc.	none	0.000	14	42	57	−6	4	63	−1	5	59	2	7	55	−2	4
38	HVW conc.	CRIMSON	0.130	Pigment suspension agglomerated in concentrate.
39	HVW conc.	APD1	0.130	Pigment suspension agglomerated in concentrate.
C24	HVW conc.	STD	0.130	26	54	52	8	7	62	−1	6	61	2	8	57	−2	5
OpC20	OpHVW conc.	none	0.000	71	77	60	11	13	62	13	12	59	14	14	58	11	11
40	OpHVW conc.	CRIMSON	0.130	81	86	54	34	14	60	26	15	57	20	14	58	15	12
C25	LCW conc.	none	0.000	Unthickened solution “runs” rather than remaining at desired thickness.
				Film thickness unknown.
41	LCW conc.	CRIMSON	0.269	Pigment appeared to agglomerate in the concentrate. Also, low viscosity
				sol'ns do not maintain desired thickness.
42	LCW conc.	APD1	0.269	Pigment appeared to agglomerate in the concentrate. Also, low viscosity
				sol'ns do not maintain desired thickness.
C26	LCW conc.	STD	0.269	Pigment did not totally disperse when added to concentrate prior to dilu-
				tion. Also, low viscosity sol'ns do not maintain desired thickness.
C27	AWL conc.	none	0.000	11	59	71	−5	6	78	0	4	78	−1	4	75	−1	4
43	AWL conc.	CRIMSON	0.130	Pigment did not disperse when added to the concentrate prior to dilution.
44	AWL conc.	APD1	0.130	Pigment did not disperse when added to the concentrate prior to dilution.
C28	AWL conc.	STD	0.130	Pigment did not disperse when added to the concentrate prior to dilution.

Examples 36, 37, and Comparative Example OpC19each contained 1.0% titanium dioxide, 0.25% red iron oxide, and 0.157% STD. The HVW base material used in Examples 38 and 39, and Comparative Example C24 contained 0.61% STD pigment solids; in these cases, 1.0 volume (Sp. grav. 1.26) of the concentrate was diluted with 3.6 volumes of water. The OpHVW base material used in Example 40 and Comparative Example OpC20 contained 0.49% TiO 2 and 0.12% red iron oxide. The LCW base material used in Examples 41, 42, and Comparative Example C26 contained 1.5% STD pigment solids; in these cases, 1.0 volume (Sp. grav. 1.40) of the concentrate was diluted with 4.0 volumes of water. The AWL base material used in Examples 43, 44, and Comparative Example C28 contained 0.685% STD pigment solids; in these cases, 1.0 volume (Sp. grav. 1.26) of the concentrate was diluted with 4.0 volumes of water.

Table 26A illustrates the visual appearance and data obtained when the color pigment is added to the fire retardant concentrate prior to preparation of the solutions. When the aqueous pigment suspension was added to the dry-powder, liquid or fluid fire retardant concentrates, the pigment particles generally agglomerated. High shear and prolonged mixing during dilution to prepare the final fire retardant solutions were unsuccessful in redispersion of the pigment agglomerates from the concentrates. Accordingly, although these samples used the aqueous pigment suspensions of the invention, their resulting fire retardant solutions, being agglomerated, are not examples of the invention.

The currently used evaluation procedures were inadequate to evaluate unthickened liquid concentrate solutions. All of the films were prepared with solutions at use-level mix concentrations. Thus, they exhibited the viscosities that the end-use fire retardants would exhibit at the time of their application to fuel or fire.

The gum thickened fire retardants generally exhibited viscosities in the range of 1000 to 1500 cps, while the unthickened liquid concentrate solutions exhibited a very low (<50 cps) viscosity. Wet films of the low viscosity solutions continued to flow after the film was prepared, thereby resulting in an unknown lower film thickness. In these cases, the film thickness gradually decreased and depended on the rate of drying.

TABLE 26B
The Impact Of The Timing Of Pigment Addition On The Opacity And Color
Of 32 Milliinch Thick Fire Retardant Films (All measurements were made on diluted
solutions. All measurements, except opacification at 2 hours, were made on dry films.)
	%	Color Characterization
			Opacification	0 Langley	6K Langley	12K Langley	18K Langley
Sample	Base	Pigment Addition	(100-Y)	Exposure	Exposure	Exposure	Exposure
Number	Material	Type	(%)	2 hrs	24 hrs.	L	a	b	L	a	b	L	a	b	L	a	b
C29	D-75 sol'n	none	0.000	15	45	62	−6	5	63	−2	5	58	2	9	52	−3	6
45	D-75 sol'n	CRIMSON	0.157	58	67	47	32	10	56	19	10	52	8	9	53	2	5
46	D-75 sol'n	CRIMSON	0.157	53	64	47	29	9	55	17	9	56	8	10	55	1	6
47	D-75 sol'n	APD1	0.157	50	68	48	33	3	57	21	9	54	9	9	54	2	5
C30	D-75 sol'n	STD	0.157	Dry pigment did not totally disperse in thickened solution, meaningful
				opacification and color measurements could not be obtained.
C31	D-75 sol'n	STD	0.157	32	53	49	13	11	59	−2	7	63	−1	10	57	−2	80
48	OpD-75	CRIMSON	0.157	82	85	53	34	11	57	23	12	58	17	12	61	12	10
	sol'n
49	C22 sol'n	CRIMSON	0.0785	53	67	47	30	13	57	11	9	56	6	11	52	0	9
50	C22 sol'n	APD1	0.0785	47	67	47	29	10	56	11	8	56	7	11	54	1	9
C32	C22 sol'n	STD	0.0785	Dry pigment did not totally disperse in thickened solution, meaningful
				opacification and color measurements could not be obtained.
51	HVW sol'n	CRIMSON	0.130	50	70	50	27	95	60	16	9	52	6	8	49	1	6
52	HVW sol'n	APD1	0.130	45	66	50	26	4	60	17	8	54	8	8	51	2	6
C33	HVW sol'n	STD	Pigment would not totally disperse in thickened solution
53	OpHVW	CRIMSON	0.130	84	86	54	34	14	59	25	15	57	19	14	57	15	13
	sol'n
54	LCW sol'n	CRIMSON	0.269	Low viscosity film “runs” resulting in unknown film thickness, measure-
				ments considered meaningless.
55	LCW sol'n	APD1	0.269	Low viscosity film “runs” resulting in unknown film thickness, measure-
				ments considered meaningless.
C34	LCW sol'n	STD	0.269	Pigment did not totally disperse when added to the diluted solution. Also,
				low viscosity sol'ns do not maintain desired thickness.
56	AWL sol'n	CRIMSON	0.130	49	78	56	35	11	76	20	9	77	7	7	75	4	7
57	AWL sol'n	APD1	0.130	43	75	56	34	4	75	18	6	76	6	5	73	3	6
C35	AWL sol'n	STD	0.130	Dry pigment did not disperse in thickened solution, meaningful
				opacification and color measurements could not be obtained.

Comparative Examples C30 and C31 were identical compositions except that while Comparative Example C30 was made in the normal manner with a propeller type agitator, Comparative Example C31 was made with additional shear agitation to more uniformly distribute the STD particles.

Examples 45 and 46 were identical compositions to each other except that the CRIMSON aqueous pigment dispersion used in Example 46 was skimmed from the top portion of the contents of a 55 gallon drum of CRIMSON that had been undisturbed for the prior 76 days. This experiment was conducted to demonstrate that the aqueous pigment dispersion is relatively stable and remains uniform when undisturbed during storage. The only slightly lower color intensities observed after about two and a half months of storage is deemed quite adequate for practical field use.

Table 26B illustrates the observations and data obtained when the color pigments were added to the fire retardant solution after dilution to end-use concentration. The aqueous pigment dispersion colorants of the invention added in this manner easily dispersed in the fire retardant solution whereas the dry-powder pigment was more difficult to disperse, particularly in the high viscosity fire retardant solutions.

Table 26A shows that the aqueously dispersed pigment, however, agglomerated in Examples 38, 39, 41, and 42, when added to the fluid and liquid concentrates. It was observed that, when added to the liquid concentrates, the pigment of the aqueous pigment suspension was attracted to the attapulgus clay and formed agglomerates that rapidly settled to the bottom of the solution. This phenomenon also occurred when the aqueous pigment suspension was added to the dilute fire retardant solutions prepared from liquid concentrates although, in that case the agglomerates were smaller and consequently settled somewhat slower to leave a clear solution above the sediment.

When the clay was omitted from the liquid concentrate formulation, however, the suspension pigment did not agglomerate—but instead remained stably dispersed throughout the diluted fire retardant solution for over 7 days. Accordingly, the liquid and fluid fire retardant concentrates, other fire retardant formulations, and ante-colorized fire retardant solutions for this invention should not contain attapulgus clay or other agglomerating constituents unless such agglomerating properties are effectively offset by other ingredients.

The above results show that the fugitive aqueous pigment dispersion/suspensions become unstable, tending to agglomerate, separate and settle from their media when added to fire retardant concentrates of all types—dry-powder, liquid or fluid types. Further, once the aqueous pigment dispersion forms agglomerates, those agglomerates resist redispersion. Consequently, fire retardant concentrates must be pre-diluted with water in order to obtain the benefits of using an aqueous pigment dispersion. The amount of dilution required can be any convenient dilution and may vary with the fire retardant type. However, the aqueous pigment dispersion/suspensions must be added to fire retardant solutions at a concentration of the fire retardant solution that won't cause agglomeration of the aqueous pigment dispersion/suspensions. It is preferred to add the aqueous pigment dispersion/suspensions to the fire retardant fluid at the fire retardant's end-use concentration.

This addition of the aqueous pigment dispersion/suspensions to the fire retardant solutions or to other ante-colorized fire retardant solutions can occur at any convenient time and by any convenient method such as, for example, by adding the aqueous pigment dispersion/suspensions to the diluted fire retardant concentrate solution via the suction-side of a transfer/recirculation pump, by adding it via suction-side addition during dilution at the aircraft loading pump, or at the pressure side.

The rate of fade of fire retardant films formed with the aqueous pigment dispersion/suspensions were slower than the films incorporating the currently used dry-powder pigment. This is advantageous since no significant fading would immediately occur after dispensing, and yet the rate of fade does occur within the current required limits.

Suspension Pigment Characteristics

Viscosity Stability of Fire Retardant Solutions

Small amounts of the CRIMSON aqueous pigment suspension was mixed with PHOS-CHEK® D-75F fire retardant solution and stored at 70° and 90° F. (21° and 32° C.) for about thirteen months. A small steel coupon was suspended in the elevated temperature samples in accordance with the U.S. Forest Service protocols (A steel coupon accelerates viscosity loss during elevated temperature storage).

Solution viscosity was measured 24 hours after the solution was prepared and then periodically through the storage period. The data, presented in Table 28 below indicate that the aqueous pigment suspension had a slightly negative impact on viscosity stability although the observed differences may be within the experimental error of the test procedure.

The specifications require that the fire retardant solution maintain ≧60% of its original viscosity when stored (with a steel coupon) for one year at ambient temperatures. The tests were conducted in Missoula, Mont. and San Dimas, Calif. However, components which are not incorporated in the stored fire retardant solution (components that are added at a time near the time of use of the fire retardant) are only required by the U.S. Forest Service to be storage stable for 30 days. Therefore, the aqueous pigment dispersions have more than adequate storage stability for the application of adding to form the colorized fire retardant solution of this invention as the delivery vehicle is being loaded.

TABLE 28
IMPACT OF FUGITIVE PIGMENT SUSPENSION
ON VISCOSITY OF D-75F SOLUTION
	%		%
Storage	Pigment	24 hr.	Viscosity Gain (+) or Loss (−) after
Temp	Add-	Visco-	30	90	180	252	388
(° F./° C.)	ition	sity*	days	days	days	days	days
72° F./21° C.	0.00	1627	1	1	1	2	2
	0.04	1607	2	1	2	3	2
	0.08	1603	2	2	2	2	1
	0.12	1600	4	2	1	3	1
90° F./32° C.**	0.00	1627	−5	−13	−24	−28	−37
	0.04	1607	−4	−17	−28	−31	−34
	0.08	1603	−3	−19	−27	−41	−44
	0.12	1600	−3	−19	−35	−40	−44
*Viscosity measured at 70-72° F. (21-22° C.) with a Brookfield Viscometer rotating at 60 rpm with No. 4 spindle.
**A small steel coupon was suspended in the samples stored at 90° F. (32° C.) to accelerate instability

Freeze-Thaw Stability of the Suspension Pigment

A study was made to determine if freezing would be a problem if containers of the neat aqueous pigment dispersion/suspension were stored outdoors at low temperatures such as might be encountered at an air tanker base during winter. It was found that the various aqueous pigment dispersion/suspension froze at or near 35° F. (2° C.). Importantly, no significant separation occurred during or following ten freeze-thaw cycles conducted over a three month period.

Pumpability

The neat aqueous pigment dispersion/suspension was pumped through an about one inch I.D. hose at rates of about 0.43 to about 1.94 gallons per minute. The following data was obtained.

Pump	CRIMSON	Water
Speed	Flow	Flow
(rpm)	(gpm)	(gpm)
100	0.43	0.43
300	1.20	1.24
500	1.94	1.90

The fugitive pigment suspension was shown to be pumpable when using a small semipositive displacement impeller pump with pumping rate equivalent to water at the same pump speed.

Other variations and modifications of this invention will be apparent to those skilled in this art after careful study of this application. This invention is not to be limited except as set forth in the following claims.

Claims

1. A method to form a colorized fire retardant composition from an ante-colorized fire retardant composition, said method comprising adding an aqueous dispersion of a non-fluorescent or fluorescent pigment to said ante-colorized fire retardant composition, in an amount effective to colorize said ante-colorized fire retardant composition, at a time proximate to discharging said colorized fire retardant composition to a fuel, wherein said aqueous dispersion is an emulsion or suspension.

2. The method to form a colorized fire retardant composition according to claim 1 further including the steps of:monitoring a parameter; and adjusting said amount responsively to said parameter.

3. The method to form a colorized fire retardant composition according to claim 1, wherein said amount is added incrementally, at a rate effective to colorize said ante-colorized fire retardant composition, as said colorized fire retardant composition is transferred to a means of delivery or as said colorized fire retardant composition is discharged from said means of delivery to said fuel.

4. The method to form a colorized fire retardant composition according to claim 3, further including the steps of:monitoring a parameter; and adjusting said rate responsively to said parameter.

5. The method to form a colorized fire retardant composition according to claims 2 or 4, wherein said parameter is a color of said fuel, a reflectance of said fuel, a color of said colorized fire retardant composition, a wind condition, a smoke condition, or an environmental temperature.

6. A method to optionally mark fuel, said method comprising:adding incrementally a colorant to a ante-colorized fire retardant composition, at a rate effective to colorize said ante-colorized fire retardant composition; discharging said colorized fire retardant composition to form a discharge; directing said discharge to mark said fuel; monitoring a parameter; and adjusting said rate responsively to said parameter.

7. The method to optically mark fuel according to claim 6, wherein said parameter is a color of said fuel, a reflectance of said fuel, a color of said colorized fire retardant composition, a wind condition, a smoke condition, or an environmental temperature.

8. A method to optically mark fuel by discharging a colorized fire retardant composition to the fuel wherein said fire retardant composition is colorized by an effective amount of an aqueous dispersion of a non-fluorescent or fluorescent pigment, having an average particle diameter less than about 1 micrometer, and wherein said aqueous dispersion is an emulsion or a suspension.

9. The method according to claim 8 wherein the fuel is timber, brush, grass, structure, or mixtures thereof.