AQUEOUS THIXOTROPES FOR WATERBORNE SYSTEMS

BACKGROUND OF THE INVENTION

1. Field of Invention:

The present invention relates to aqueous thixotropes for waterborne systems and, more particularly, to aqueous dispersions of fumed silica for use as effective thixotropes and rheology control agents in waterborne systems.

2. Description of the Related Art:

Both hydrophilic and hydrophobic fumed silicas are widely used in the coating industry to improve rheology, for flow control and storage stability, as well as serve as an anti-settling agent for pigments and fillers. The production of hydrophilic fumed silica is a well known process. Grades vary in particle and aggregate size. Hydrophobic silica can be produced by treating a fumed silica with a suitable agent which will vary depending on the desired degree of hydrophobicity and other characteristics. Such treating agents include, for example, polydimethylsiloxane oils of various molecular weights, dimethyldichlorosilane, trimethoxyoctylsilane, disilazanes, such as hexamethyldisilazane (HMDZ),and mixtures thereof.

In aqueous systems, which include both emulsions and water reducible vehicles, untreated (hydrophilic) silicas are typically not effective because of the large concentrations of silica that are necessary to realize the desired thickening. However, methods exist for increasing the thickening capability of a given concentration of silica by using certain substances as additives to modify the nature of the system. For example, in systems that are not readily responsive to fumed silica because of inherent chemical properties, the correct additive can often facilitate efficient viscosity and thixotropic control. For example, in highly hydrogen-bonding liquids, the additives that are typically most useful in improving the thickening and thixotropic efficiency of fumed silica are cationic surfactants. The surfactants modify and partially impede the interaction between fumed silica and the solvent, thereby allowing the fumed silica network structure to

develop, thus resulting in improved viscosity, thixotropy, and suspending properties. In non- hydrogen-bonding liquids, the additives which prove most useful are short chain molecules with more than one functional group capable of hydrogen bonding, such as glycols. These molecules act as bridging compounds between the surface hydroxyls of fumed silica aggregates, which form chains consisting of alternating silica aggregates and organic molecules. Such systems require the separate addition of certain additives to untreated silica dispersions.

As environmental awareness increases, manufacturers face increased pressure to replace conventional solvent based systems. As a result, aqueous systems are increasingly used in many applications such as automotive and industrial coatings, paints, inks, adhesives, and the like. While hydrophilic and hydrophobic silicas have both been used in solvent-based coating formulations on a commercial scale, their use in aqueous formulations have been plagued with disadvantages. For example, in aqueous systems, either the silica additive must be increased to unacceptable levels or the formulation does not attain the desired level of performance. A demand, therefore, exists for aqueous systems which perform comparably to solvent based systems and, accordingly, for improved additives or methods to accomplish such results.

It is therefore an object of the present invention to provide a versatile and efficient rheological additive for waterborne systems, such as in coatings and other industrial applications.

A further object is to provide an additive that fosters stability in aqueous compositions. A still further object is to provide a thixotrope which alleviates many of the waterborne coating rheology control formulating difficulties that exist with other inorganic and organic materials .

SUMMARY OF THE INVENTION

Accordingly, the present invention is directed to an aqueous dispersion of fumed silica that provides enhanced rheology control and thixotropy to waterborne systems. The fumed silica dispersion is uniformly dispersed in the waterborne system such that an amount ranging between 0.5 % and 10.0 % , by weight, of silica is present in the final composition. The waterborne system, therefore, includes an aqueous dispersion of fumed silica, and a waterborne resin. The resin is selected from the group consisting of alkyd, acrylic, polyester, polyether, silicate, urethane, epoxy, formaldehyde, vinyl, and mixtures thereof. The fumed silica has a surface area between about 85 m ² /g and about 410 m ² /g.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a graph of the rheological performance of an epoxy resin system incorporating the present fumed silica dispersion;

FIG. 2 is a graph of the rheological performance of an bisphenol-A epoxy resin system incorporating the present fumed silica dispersion;

FIG. 3 is a graph of the rheological performance of an epichlorohydrin and bisphenol-A resin system incoφorating the present fumed silica dispersion;

FIG. 4 is a graph of the rheological performance of a urethane modified epoxy resin system incoφorating the present fumed silica dispersion; and FIG. 5 is a graph of the rheoiogical performance of an acrylic resin system incoφorating the present fumed silica dispersion; and

FIG. 6 is a graph of the response of the present fumed silica dispersion in a typical water reducing alkyd coating formulation.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is directed to an aqueous dispersion of hydrophilic fumed silica which provides enhanced rheology control and thixotropy to aqueous or waterborne systems. The present aqueous dispersion of fumed silica is effective in alkyd, acrylic, polyester, polyether, silicate, urethane, epoxy, formaldehyde, vinyl, and mixtures or modifications thereof as vehicle systems. It has been found that unlike other organic and inorganic materials used as thixotropes in waterborne systems such as coatings, the present aqueous dispersion of fumed silica will not typically react with additives in the formulation to produce unexpected side effects after product manufacture.

Fumed silicas useful in this invention are generally characterized by a chain-like structure having high surface area per unit weight. The production of fumed silica is a well-documented process which involves the hydrolysis of silicon tetrachloride vapor in a flame of hydrogen and oxygen. Molten particles of roughly spherical shapes are formed in the combustion process, the diameters of which are varied through process parameters. These molten spheres of fumed silica, typically referred to as primary particles, fuse with one another by undergoing collisions at their contact points to form branched, three dimensional chain-like aggregates. The force necessary

to break aggregates is considerable and often considered irreversible because of the fusion. During cooling and collecting, the aggregates undergo further collision that may result in some mechanical entanglement to form agglomerates. Compared to the aggregates where the primary particles are fused together, agglomerates are thought to be loosely held together by Van der Waals forces and can be reversed, i.e. de-agglomerated, by proper dispersion in suitable media.

The size of the primary spherical particles that comprise the fumed silica aggregates determine the surface area. The surface area of the fumed silica, as measured by the nitrogen adsoφtion method of S. Brunauer, P. H. Emmet, and I. Teller, J. Am. Chemical Society, Volume 60, Page 309 (1938) and commonly referred to as BET, typically ranges from about 85 m ² /g to about 410 πr/g. In the present invention, the fumed silica is preferably in a range from about 175 m ² /g to about 225 m ² /g, and are of a high purity. High purity means that the total impurity content is typically less than 1 % and preferably less than 0.01 % (i.e., 100 ppm). Although many commercially available fumed silicas are suitable, CAB-O-SIL ^® fumed silica, available from the Cab-O-Sil Division of Cabot Coφoration, Tuscola, IL, having a surface area of about 200 m ² /g is most preferred. Such a silica has been found to be of high quality and is readily dispersable.

The fumed silica of the present invention is uniformly dispersed in a stable aqueous medium (e.g. deionized water) using conventional methods known to those skilled in the art. By uniformly dispersed is meant that the aggregates are isolated and well distributed throughout the medium. By stable is typically meant that the aggregates will not re-agglomerate and settle out (e.g. form a hard, dense sediment). The fumed silica dispersion should have a pH between 5.0 and 10.5 and may be adjusted by the addition of a suitable base such as sodium hydroxide, potassium hydroxide, ammonia and the like. Preferably, the fumed silica dispersion of the present invention has a pH ranging between 7.0 and 9.5. The fumed silica dispersion of the present invention is preferably prepared by the method described by Miller et al., in U.S. Patent No. 5,246,624, the disclosure of which is incoφorated herein in its entirety by reference. Although many commercially available fumed silica dispersions are suitable, CAB-O-SPERSE ^® aqueous fumed silica dispersions, available from the Cab-O-Sil Division of Cabot Coφoration, Tuscola, IL, are most preferred.

The waterborne systems of the present invention are prepared by combining or mixing the aqueous dispersions of fumed silica directly with a waterborne resin, such as an alkyd, acrylic,

polyester, silicate, urethane, epoxy, and the like, or with a formulation containing a waterborne resin under low shear conditions (i.e., to prevent foaming) until a uniform homogeneous composition is obtained. Typically, the fumed silica dispersions range from about 10% to about 45 % solids, by weight; and, preferably, between 15% and 30% solids, by weight. Most preferably, a fumed silica dispersion of about 20 % solids, by weight, has been found to maximize the loading level of silica while maintaining the colloidal stability of the dispersion.

The aqueous dispersions of fumed silica of the present invention are useful in aqueous systems to provide effective rheological control (i.e., viscosity and thixotropy) for example, in industrial and automotive coating, adhesive, paint, and ink applications. It has been found that another advantage of using an aqueous dispersion of fumed silica in waterborne resin systems is to provide rheology and sag control, and anti-settling. It is also believed that a stable matrix is formed in waterborne formulations after the incoφoration of the fumed silica dispersion due to electrostatic interaction. During the high-shear processes usually found in product application, the matrix disintegrates, thereby reducing viscosity and permitting near-Newtonian flow. After application, the inorganic matrix reforms at a predictable rate to provide resistance to sagging and edge-pull during film coalescence and/or cure. This matrix remains unmodified through the many physical film changes during conversion from liquid to solid, thus providing a predictable application consistency.

The aqueous dispersion of fumed silica has been found to be an effective suspension agent in some formulations due to its internally-generated structure. The product forms a matrix capable of stopping or significantly retarding undesirable striation and pigment settling, even in products containing powdered zinc or other unusually heavy pigments. It is noted that the addition of dry hydrophilic fumed silica to waterborne systems has been found to be ineffective as a rheology control agent. In particular, the viscosity of the system will tend to continually increase over time, thereby not achieving stability. In addition, the dry silica is difficult to handle and disperse, and may tend to settle out at higher loading levels.

Other advantages of the present dispersions are that they will not migrate in wet or dry films and are unaffected by heat and atmospheric exposure in the dried/cured film. The dispersion is inherently non-yellowing and will not contribute to color changes or drift in either

the wet or dry state. Moreover, the present aqueous dispersions of fumed silica are biologically inactive and is not expected support microbial activity.

The present aqueous dispersions of fumed silica used as aqueous thixotropes in water based systems are responsive to changes in pH, but have been found to be effective in the 7.0 to 9.5 pH range commonly used in products formulated for industrial and commercial use. The present dispersions have also been found to be effective in higher pH ranges, depending specifically upon the individual formulation.

Although the loading level, as a percent of total or resin solids, the precise method of incoφoration, and the stage of manufacture at which this is accomplished, all play a significant role in the final effectiveness of the dispersion, the aqueous dispersion of fumed silica of the present invention has been shown to be effective in many systems used in formulating waterborne products.

The present invention will be further illustrated by the following examples, which are intended to be illustrative in nature and are not to be considered as limiting the scope of the invention.

EXAMPLE I

An aqueous colloidal dispersion of fumed silica, which can be used as an aqueous thixotrope in the present invention, was prepared and evaluated as follows.

Approximately 205.24 grams of deionized water and 0.4 gram of 38% hydrochloric acid were added to a commercial Waring blender. While mixing, 80 grams of CAB-O-SIL ^® PTG grade fumed silica were added to the blender. When the addition was complete, the mixture was stirred at a high rate for about five minutes. After the stirring was completed, about 108.52 grams of water were added to the mixture followed by about 6.12 grams of a 10% potassium hydroxide solution stabilizer. After the addition of the stabilizer, the mixture was stirred for an additional two minutes. The aqueous fumed silica dispersion prepared had a 20% solids level, a viscosity of about 65 centipoise, and a pH of 9.

EXAMPLE II

A scaled-up volume of the dispersion of EXAMPLE I was prepared, using 2-amino-2- methyl-1 -propanol, available as AMP-95™ from Angus Chemical Company, Buffalo Grove, IL, as the base-stabilizer. Approximately 1283.80 grams of water were mixed with 0.251 gram of 38 % hydrochloric acid. About 499.92 grams of CAB-O-SIL ^® PTG grade fumed silica were then added to the water/acid mixture, and was stirred for about 20 minutes. 678 grams of deionized water was then added to the mixture, followed by 10.54 grams of the AMP-95™ stabilizer. The aqueous fumed silica dispersion prepared had a 20.22% solids level, and a pH of 9.

EXAMPLE III

A waterborne system, including an aqueous fumed silica dispersion (similar to the dispersion prepared in EXAMPLE I) and a waterborne epoxy resin, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope for waterborne systems. The aqueous fumed silica dispersion was mixed with Wateφoxy ^® 701 Resin epoxy curing agent, available from Henkel Coφoration, Ambler, PA, until a loading level of 2% dry silica on resin solids was achieved. The viscosity (centipoise), shear thinning index (STI), and pH were then measured after sample preparation (0 days), and after periods of 1 and 7 days. The viscosity was measured on a Brookfield viscometer using Nos. 3 or 4 spindle at 6 and 60 RPM's. The experimental results are presented below in Table 1.

TABLE 1

DAYS 0 1 7

VISCOSITY

Sample 1, 6 RPM 1500 1500 1500

Sample 1, 60 RPM 1442 1442 1442

Sample 2, 6 RPM 3300 3900 3800

Sample 2, 60 RPM 1990 2540 2590

STI

Sample 1 1.04 1.04 1.04

Sample 2 1.66 1.53 1.51

pH

Sample 1 11.33 11.33 11.33

Sample 2 11.29 11.41 10.99

FIG. 1 is a graph of the viscosity of a control sample (Sample 1), a waterborne epoxy resin without a rheology control agent, versus the present waterborne system (Sample 2) over time. Both Table 1 and FIG. 1 illustrate that the present waterborne system achieved stable performance after about 1 day and a desired increase in viscosity.

EXAMPLE IV

A waterborne system, including an aqueous fumed silica dispersion (similar to the dispersion prepared in EXAMPLE I) and a waterborne bisphenol-A epoxy resin, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope for waterborne systems. The aqueous fumed silica dispersion was mixed with EPI-REZ ^® 3510-W-60 nonionic, aqueous dispersion of bisphenol-A epoxy resin, available from Shell Chemical Co. , Houston, TX, until a loading level of 2% dry silica on resin solids was achieved. The viscosity (centipoise), shear thinning index (STI), and pH were then measured after sample preparation (0 days), and after periods of 1 and 7 days. The viscosity was measured on a Brookfield viscometer using Nos. 3 or 4 spindle at 6 and 60 RPM's. The experimental results are presented below in Table 2.

TABLE 2

DAYS 0 1 7

VISCOSITY

Sample 1 , 6 RPM 220 220 220

Sample 1, 60 RPM 178 178 178

Sample 2, 6 RPM 520 500 400

Sample 2, 60 RPM 264 270 260

STI

Sample 1 1.24 1.24 1.24

Sample 2 1.97 1.85 1.85

pH

Sample 1 3.41 3.41 3.41

Sample 2 5.70 7.04 7.04

FIG. 2 is a graph of the viscosity of a control sample (Sample 1), a waterborne bisphenol-A epoxy resin without a rheology control agent, versus the present waterborne system

(Sample 2) over time. Both Table 2 and FIG. 2 illustrate that the present waterborne system achieved stable performance, particularly the Sample 2 measured at 60 RPM, and a desired increase in viscosity. The Sample 2 viscosity measured at 6 RPM decreased more rapidly.

EXAMPLE V

A waterborne system, including an aqueous fumed silica dispersion (similar to the dispersion prepared in EXAMPLE I) and a waterborne epichlorohydrin and bisphenol-A epoxy resin, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope for waterborne systems. The aqueous fumed silica dispersion was mixed with EPI- REZ ^® 3510-WY-55 (55% solids) dispersion of Econ™ 1001F condensation product of epichlorohydrin and bisphenol-A in water, available from Shell Chemical Co. , Houston, TX, until a loading level of 2% dry silica on resin solids was achieved. The viscosity (centipoise), shear thinning index (STI), and pH were then measured after sample preparation (0 days), and after

periods of 1 and 7 days. The viscosity was measured on a Brookfield viscometer using Nos. 3 or 4 spindle at 6 and 60 RPM's. The experimental results are presented below in Table 3.

TABLE 3

DAYS 0 1 7

VISCOSITY

Sample 1 , 6 RPM 2700 2700 2700

Sample 1, 60 RPM 1010 1010 1010

Sample 2, 6 RPM 3000 5600 15400

Sample 2, 60 RPM 1130 1950 3700

STI

Sample 1 2.67 2.67 2.67

Sample 2 2.65 2.87 4.16

pH

Sample 1 8.74 8.74 8.74

Sample 2 9.38 9.36 7.40

FIG. 3 is a graph of the viscosity of a control sample (Sample 1), a waterborne epichlorohydrin and bisphenol-A epoxy resin without a rheology control agent, versus the present waterborne system (Sample 2) over time. Both Table 3 and FIG. 3 illustrate that the present waterborne system achieved a desired increase in viscosity while providing semi-stable performance in thixotropy. The Sample 2 viscosity measured 6 RPM increased rapidly. The Sample 2 measured at 60 RPM increased less rapidly and was more stable.

EXAMPLE VI

A waterborne system, including an aqueous fumed silica dispersion (similar to the dispersion prepared in EXAMPLE I) and a waterborne urethane modified epoxy resin, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope for waterborne systems. The aqueous fumed silica dispersion was mixed with EPI-REZ ^® 5520- W-60 nonionic aqueous dispersion of urethane modified epoxy resin, available from Shell Chemical Co., Houston, TX, until a loading level of 2% dry silica on resin solids was achieved. The viscosity (centipoise), shear thinning index (STI), and pH were then measured after sample preparation (0 days), and after periods of 1 and 7 days. The viscosity was measured on a Brookfield viscometer using Nos. 3 or 4 spindle at 6 and 60 RPM's. The experimental results are presented below in Table 4.

TABLE 4

DAYS 0 1 7

VISCOSITY

Sample 1, 6 RPM 5600 5600 5600

Sample 1, 60 RPM 1440 1440 1440

Sample 2, 6 RPM 29450 17200 17900

Sample 2, 60 RPM 3710 2730 2920

STI

Sample 1 3.89 3.89 3.89

Sample 2 7.94 6.30 6.13

pH

Sample 1 3.51 3.51 3.51

Sample 2 7.37 7.53 7.40

FIG. 4 is a graph of the viscosity of a control sample (Sample 1), a waterborne urethane modified epoxy resin without a rheology control agent, versus the present waterborne system (Sample 2) over time. Both Table 4 and FIG. 4 illustrate that the present waterborne system achieved stable performance after about 1 day and a desired increase in viscosity.

EXAMPLE VII

A waterborne system, including an aqueous fumed silica dispersion (similar to the dispersion prepared in EXAMPLE I) and a waterborne acrylic copolymer resin, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope for waterborne systems. The aqueous fumed silica dispersion was mixed with Neocryl ^® A-639 waterborne acrylic copolymer, available from Zeneca Resins, Wilmington, MA, until a loading level of 2% dry silica on resin solids was achieved. The viscosity (centipoise), shear thinning index (STI), and pH were then measured after sample preparation (0 days), and after periods of 1 and 7 days. The viscosity was measured on a Brookfield viscometer using Nos. 3 or 4 spindle at 6 and 60 RPM's. The experimental results are presented below in Table 5.

TABLE 5

DAYS 0 1 7

VISCOSITY

Sample 1, 6 RPM 480 480 480

Sample 1, 60 RPM 212 212 212

Sample 2, 6 RPM 540 680 580

Sample 2, 60 RPM 254 282 258

STI

Sample 1 2.26 2.26 2.26

Sample 2 2.13 2.41 2.25

pH

Sample 1 6.53 6.53 6.53

Sample 2 6.59 6.49 6.53

FIG. 5 is a graph of the viscosity of a control sample (Sample 1), a waterborne urethane modified epoxy resin without a rheology control agent, versus the present waterborne system (Sample 2) over time. Both Table 5 and FIG. 5 illustrate that the present waterborne system achieved stable performance after about 1 day and desired increase in viscosity.

EXAMPLE VIII

A coating formulation, incoφorating the aqueous fumed silica dispersion of the present invention, a waterborne acrylic resin system, and various additives, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope in coatings. A high gloss waterborne topcoat, based on Neocryl ^® XK90 acrylic copolymer emulsion, available from Zeneca

Resins, Wilmington, MA, was prepared. The coating formulation, as set forth below in Table

6, was prepared by first mixing the components of Part A in a Waring Blender at high speed for about 5 minutes. The Part B components were then added and dispersed into the Part A mixture in the Waring Blender at high speed for about 5 minutes. The viscosity (mPas), STI, and pH were then measured after periods of 2 days, 25 days, and 60 days. These measurements were taken for a high gloss aqueous top coat formulation without any commercial thickening agent

(Control), and a similar formulation utilizing an aqueous fumed silica dispersion (similar to the dispersion prepared in Example I) as an aqueous thixotrope (Sample). The viscosity of the coatings was measured on a Brookfield Rotary Viscometer RVD-II using spindle Nos. 1 or 2 at speeds of 0.5, 1.0, 2.5, 5.0, and 10.0 RPM. The STI is a ratio of the measured viscosity at 0.5 and 5.0 RPM's. The experimental results are presented below in Table 7.

TABLE 6

FORMULATION CONTROL SAMPLE (WT. %) (WT. %)

Part A:

Deionized water 4.96 0.94

Neocryl ^® XK90 acrylic 23.65 23.56 dispersion

Dehydran™ 1293 defoamer 0.30 0.30 (Henkel)

Disperse™ Ayd W22 0.34 0.34 dispersant (Daniel)

Aqueous Fumed Silica — 5.00 Dispersion (i.e., Example I)

Butyl Glycol-coalescent 1.78 1.77

TiO ₂ 18.78 18.78

Part B:

Butyl Glycol 1.78 1.78

Neocryl ^® XK90 48.0 47.10

NaNO ₂ , 30% sol'n.-rust 0.41 0.41 inhibitor

100.00 100.00

TABLE 7

DAYS 2 25 60

VISCOSITY (mPas)

Control, 0.5 RPM 100 90 70

1.0 RPM 90 60 70

2.5 RPM 72 58 56

5.0 RPM 66 54 56

10.0 60 52 55 RPM

Sample, 0.5 RPM 2560 1280 1280

1.0 RPM 1720 1040 1080

2.5 RPM 1010 752 784

5.0 RPM 720 620 648

10.0 524 508 536 RPM

STI (0.5/5.0 RPM)

Control 1.52 1.66 1.25

Sample 3.56 2.06 1.98

As illustrated above, the aqueous dispersion of the present invention can be incoφorated not only in resins but also in coating formulations.

EXAMPLE IX

A coating formulation, incoφorating the aqueous fumed silica dispersion of the present invention, a waterborne alkyd resin system, and various additives, was prepared and evaluated to determine the effectiveness of the present dispersion as a thixotrope in coatings. An aqueous industrial maintenance coating based on Resydrol ^® AY 466 W, 38% , alkyd resin emulsion, available from Hoechst Celanese, Fine Chemicals Division, Charlotte, NC, was prepared. The coating formulation, as set forth below in Table 8, was prepared by mixing the components in a Waring blender at high speed for about 5 minutes. The viscosity (mPas) and STI were then measured after periods of 1, 18 and 60 days. These measurements were taken for an aqueous industrial maintenance coating of formulation with and without a commercial thickening agent (Borchigel™ L75N, 54%), and a similar formulation utilizing an aqueous fumed silica dispersion (similar to the dispersion prepared in Example 1) as an aqueous thixotrope (Sample). The viscosity of the coatings was measured on a Brookfield Rotary Viscometer. The experimental results are presented below in Table 9. FIG. 6 is a graph illustrating the viscosity aging over time, taken from the data in Table 9, and corresponding to a shear rate of 1.4 dynes/sec. At a finess of grind <10 microns (the graph was converted from mPas to centipoise). As illustrated in FIG. 6, the aqueous fumed silica dispersion achieved and maintained a stable workable viscosity for an extended period of time. The Control sample exhibited a high initial increase in viscosity and substantial loss over time.

TABLE 8

FORMULATION CONTROL SAMPLE

(WT. %) (WT. %)

Resydrol ^® AY466 W,38% 70.00 69.02

Aqueous Ammonia, 10% 3.00 2.96

Additol™ VXW 4940 drying 1.30 1.28 agent (Hoechst Celanese)

Titanox™ 2300 (Kronos) 21.24 20.94

Borchigel™ L7SN, 54% 1.86 — thickener

Aqueous Fumed Silica — 4.81 Dispersion (i.e. , Example I)

Additol™ VXW 4973 0.30 0.30 defoamer

Surfynol™ SE-F wetting 0.30 0.30 agent (Air Products)

Additol™ XL 297 0.40 0.39 antiskinning agent

Deionized water 1.60 —

100.00 100.00

TABLE 9

1 18 60

DAYS

VISCOSITY

Control 6.660 4.340 3.472

Control without 0.785 0.588 0.588

Borchigel™ thickener

Sample 1.985 2.940 3.087

STI

Control 1.54 1.27 1.66

Control without 3.13 1.81 1.88 thickener

Sample 3.33 4.64 2.63

As illustrated above, the aqueous dispersion of the present invention can be incoφorated not only in resins but also in coating formulations.

Although particular embodiments of the invention have been described in detail for puφoses of illustration, various changes and modifications may be made without departing from the scope and spirit of the invention. Accordingly, die invention is not to be limited except as by the appended claims.

What is claimed is: