Stable mixtures containing opacifying pigments

Abstract
A number of stable opacifying mixtures are disclosed which contain specific combinations and levels of titanium dioxide, thickeners, and dispersants. These stable mixtures may be employed in a method of making paints using prepaints or as a conventional component in a coating such as a paint, or in other end-uses where opacifying pigments are employed.
Description
BACKGROUND OF THE INVENTION

1. Field of the Invention


This invention is related to stable mixtures containing opacifying pigments and more specifically, to stable mixtures containing select combinations and levels of titanium dioxide, a thickener, and a dispersant for use in making paint and other end products.


2. Description of Related Art


In co-pending U.S. provisional patent applications Ser. Nos. 60/183,655; 60/183,656; and 60/247,639; prepaints and a method of making paints from these prepaints is described. One of the prepaints is a mixture comprising at least one opacifying pigment, typically titanium dioxide. The other two prepaints may contain either an extender pigment or/and an emulsion polymeric binder. A key requirement for the prepaints is their compatibility with one another so that they may be mixed with each other in various ratios to make at least one paint line. Another key requirement is that the prepaints, whether comprising an opacifying pigment, an extender pigment, or an emulsion polymeric binder, be stable so that the prepaints may be prepared, shipped, and stored without failing, for example, failure by exhibiting non-homogeneity, syneresis, settling, gelling and/or viscosity changes.


With respect to prepaints containing an opacifying pigment, stability can be a serious problem. This is especially true when one considers that even the best commercially-available titanium dioxide slurries show some syneresis (>2% by volume by visual inspection) upon storage and must be stirred vigorously and for a considerable length of time before use.


Hence, there is a need for stable mixtures containing specific combinations and levels of titanium dioxide, thickeners, and dispersants that may be employed, inter alia, as prepaints in a method of making paints or as conventional components in other end-uses where opacifying pigments are employed, including coatings, impregnants, inks, graphic arts, papers, textiles, caulks, mastics, adhesives, sealants, building products and leather.


SUMMARY OF THE INVENTION

Various fluid opacifying mixtures based on titanium dioxide are provided. Some of the mixture are stable and no mixing is required, others are stable with occasional mixing required, and others are stable with constant mixing required.


As used herein for all the mixtures “lbs/100 gallons” is based on the weight of the dry material, unless otherwise noted.


The following mixtures are stable and require no mixing when formulated as described below.


Mixture is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.2 to about 20 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener selected from the group consisting of:
    • (i) a HEUR having a C4-C12 hydrophobe and a molecular weight of about 10,000 to about 200,000;
    • (ii) a HEUR having a C6-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000; and
    • (iii) combinations thereof; and
  • (c) about 1.5 to about 16 lbs/100 gallons of at least one dispersant selected from the group consisting of a maleic acid/diisobutylene copolymer, a butylmethacrylate/methacrylic acid copolymer, and an acrylic acid—hydroxypropyl acrylate copolymer;


Mixture 2 is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one interior-grade titanium dioxide;
  • (b) about 0.3 to about 5 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; and
  • (c) about 1.8 to about 23 lbs/100 gallons of at least one dispersant selected from the group consisting of maleic acid/diisobutylene copolymer, a butylmethacrylate/methacrylic acid copolymer, and an acrylic acid—hydroxypropyl acrylate copolymer;


Mixture 3 is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one interior-grade titanium dioxide;
  • (b) about 0.5 to about 3 lbs/100 gallons of at least one hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; and
  • (c) about 1.8 to about 23 lbs/100 gallons of at least one polyacrylic acid dispersant.


Mixture 4 is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 2 to about 6 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; and
  • (c) about 1.8 to about 23 lbs/100 gallons of at least one polyacrylic acid dispersant.


Mixture 5 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.2 to about 10 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000;
  • (c) about 2 to about 10 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000; and
  • (d) about 3.0 to about 22.5 lbs/100 gallons of at least one maleic acid/diisobutylene copolymer dispersant.


Mixture 6 is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.2 to about 10 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000;
  • (c) about 2 to about 10 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000; and
  • (d) about 0.5 to about 22.5 lbs/100 gallons of at least one acrylic acid—hydroxypropyl acrylate dispersant.


The following mixtures are stable with occasional mixing required.


Mixture 7 is a fluid opacifying pigment mixture comprising:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 1 to about 10 lbs/100 gallons of at least one hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,0000 or hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000;
  • (c) optionally, about 2 to about 12 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000 or at least one clay thickener; and
  • (d) about 0.5 to about 22.5 lbs/100 gallons of at least one acrylic acid/hydroxyl propyl acrylate dispersant.


Mixture 8 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.3 to about 5 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; and
  • (c) about 1.2 to about 45 lbs/100 gallons of at least one polyacrylic acid dispersant.


The following mixtures are stable with constant mixing required. They are formulated as described below.


Mixture 9 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.5 to about 10 lbs/100 gallons of at least one hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,0000 or about 0.5 to about 10 lbs/100 gallons of a hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; and
  • (c) about 1.2 to about 18 lbs/100 gallons of at least one maleic acid/diisobutylene dispersant.


Mixture 10 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.1 to about 3 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; and
  • (c) about 0.6 to about 22.5 lbs/100 gallons of at least one acrylic acid/hydroxyl propyl acrylate dispersant.


Mixture 11 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide;
  • (b) about 0.1 to about 3 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; and
  • (c) about 0.6 to about 45 lbs/100 gallons of at least one maleic acid/diisobutylene dispersant.


Mixture 12 is a fluid opacifying pigment mixture containing:

  • (a) about 600 to about 1500 lbs/100 gallons of at least one interior-grade titanium dioxide;
  • (b) about 0.2 to about 20 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide urethane polymer (HEUR) thickener selected from the group consisting of:
    • (i) a HEUR having a C4-C12 hydrophobe and a molecular weight of about 10,000 to about 200,000;
    • (ii) a HEUR having a C6-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000; and
    • (iii) combinations thereof; and
  • (c) about 1.2 to about 8 lbs/100 gallons of at least one maleic acid/diisobutylene dispersant.


All of the above mixtures have a titanium dioxide (TiO2) pigment volume concentration (PVC) of about 40 to 100%, a titanium dioxide (TiO2) volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU.


All of the mixtures contain water and may contain optional additives selected from the group consisting of a defoamer, a surfactant, a coalescent, a base, a biocide, a mildeweide, a co-dispersant, a polymeric binder, a voided latex polymer and combinations thereof.


In order to prepare stable mixtures of opacifying pigments, one must follow strict rules in selecting the types and level of specific ingredients, using the general approach set out below:

    • select the type and level of titanium dioxide based on whether the final paint will be for exterior or interior use with a universal-grade being selected for interior, exterior, or interior/exterior use and with an interior-grade being selected for interior use only;
    • select the appropriate rheology modifier/thickener based on the type of titanium dioxide selected;
    • select the appropriate dispersant based on the type of rheology modifier/thickener selected;
    • determine the level of dispersant necessary to produce a stable final mixture; and
    • determine the level of rheology modifier/thickener required to produce a stable final mixture.


As used herein, the term “stable” applies to those mixtures that meet all of the following criteria, as set out in the Stability Tests described below, after being stored at a temperature of at least 120° C. for at least ten (10) days:

    • (1) there is less than 2% by volume of syneresis in the mixture (determined by inspecting the pigment mixture visually) (referred to herein as “Stability Test 1”).
    • (2) the mixture has a Brookfield viscosity (measured at a shear rate of 1.25 sec−1) of less than 100,000 centipoise, preferably less than 50,000 centipoise after cooling to ambient temperature (22-25° C.), but prior to mechanical shearing (referred to herein as “Stability Test 2”).
    • (3) the ratio of the Brookfield viscosity (measured at a shear rate of 1.25 sec−1) after heat aging to the Brookfield viscosity (measured at a shear rate of 1.25 sec−1) prior to heat aging is no greater than 3 after the mixture is cooled to ambient temperature (22-25° C.) and after mechanical shearing using a propeller-type mixer (referred to herein as “Stability Test 3”). Commercial titanium dioxide slurries do not pass Stability Test 1 and must be stirred, sometimes constantly, prior to use. Mixtures having Brookfield viscosities higher than those specified in Stability Test 2 tend to gell and resist flow and therefore are difficult to pump in conventional equipment. Stability Test 3 is used to determine whether or not the mixture developed, or will develop, a gel network resistant to shear thinning (mixing) during storage.


The mixing conditions used to categorize the stability of the fluid opacifying pigment mixtures are as follows:

  • (1) mixtures which require no mixing or other form of agitation over typical storage times (at least 30 days) and under storage conditions where the temperature can be as high as 140° F. and as low as 25° F. to remain stable are referred to herein as “stable with no mixing required”)(require mixing over 0% of storage time);
  • (2) mixtures which require periodic or occasional mixing or other forms of agitation to re-homogenize or break any minimal or slight structure formed over the typical storage times and conditions described above are referred to herein as “stable with occasional mixing required”)(require mixing over >0% of storage time); and
  • (3) mixtures which require constant mixing or other forms of agitation to re-homogenize or break any significant structure formed over the typical storage times and conditions described above (are referred to herein as “stable with constant mixing required”)(require mixing over >50% of storage time).


    It should be noted that while the “stable with no mixing required” condition requires no mixing or other form of agitation to remain stable, applying some form of mixing or agitation to the mixture (whether occasional or constant) does not exclude that particular mixture from the definition of a stable mixture with “no mixing required”. Likewise, it should be noted that while the “stable with occasional mixing required” condition requires only occasional mixing or other form of agitation to remain stable, applying constant mixing or agitation to the mixture does not exclude that particular mixture from the definition of a stable mixture with “occasional mixing required”.


Any type of mixer or agitator may be used such as, but not limited to an impellar, a recirculator, a shaker, a mill, a rotator, a bubbler, a sonicator, a pump or a like means suitable to move the mixture about itself.


The mixtures herein may be employed as prepaints in systems using delayed product differentiation as described in U.S. patent applications Ser. No. 60/183,655 filed Feb. 18, 2000; Ser. No. 60/183,656 filed Feb. 18, 2000; Ser. No. 60/247,639 filed Nov. 10, 2000], as well as employed as replacements for conventional mixtures containing opacifying pigments, such as titanium dioxide slurries, mill bases, colorant dispersions, coating colors, and the like.


The pigment volume concentration (PVC) is a measure of how “binder-rich” a formulation is. It is calculated using the formula:
PVC(%)=(volumeofpigment(s)+volumeextender(s))(volumeofpigment(s)+volumeextender(s)+volumebinder(s)×100


The volume solids content (VS) is the dry volume of pigment(s) plus the dry volume of extender(s) plus the dry volume of binder(s). It is calculated using the formula:
VS(%)=dryvolumeofpigment(s)+dryvolumeofextender(s)+dryvolumeofbinder(s)totalvolumeofformulation×100.


If additives are present, their volumes are not included in determining the total dry volume.


The titanium dioxide pigment volume concentration (TiO2 PVC) is a measure of how “binder-rich” a formulation is relative to only the titanium dioxide (TiO2) content. It is calculated using the formula:
TiO2PVC(%)=volumeofTiO2pigment(s)(volumeofpigment(s)+volumeextender(s)+volumebinder(s)×100


The titanium dioxide volume solids content (TiO2 VS) is the dry volume of TiO2 pigment(s) plus the dry volume of extender(s). It is calculated using the formula:
TiO2VS(%)=dryvolumeofTiO2pigment(s)totalvolumeofformulation×100.

If additives are present, their volume is not included in determining the total dry volume.


Opacifying Pigments


Suitable opacifying pigments include:

  • (1) white pigments which impart white scattering power to a paint across all visible wave lengths without a high degree of absorption; and
  • (2) auxiliary hiding pigments including inorganic and organic solids or voided latex polymers which do not impart a primary color or hiding power to a paint although they may have secondary influences on those properties.


Such opacifying pigments include titanium dioxide or a combination of titanium dioxide and auxiliary hiding pigments such as voided latex polymer particles, zinc oxide, lead oxide, a synthetic polymer pigment, and mixtures thereof. Rutile and anatase grades of titanium dioxide are suitable for use herein. Rutile titanium dioxide is preferred. The surface of the titanium dioxide may be treated with various organic or inorganic surface treatments, e.g., the oxides of silica, alumina, and zirconia. Fumed titanium oxide is also useful herein.


For specific mixtures, certain grades of titanium dioxide are required. For example, for some of the mixtures universal-grade titanium dioxide may be used, whereas for others interior-grade titanium dioxide must be used. As used herein, “universal-grade” titanium dioxide means titanium dioxide that is suitable for use in both interior and exterior applications and which is typically treated with oxides of alumina (about 1 to about 7%), silica (up to about 15%) and zirconia (up to about 15%). As used herein, “interior-grade” titanium dioxide means titanium dioxide that is only suitable for use in interior applications which is typically treated with only the oxides of alumina (about 1 to about 7%) or a combinations of the oxides of alumina (about 1 to about 7%) with the oxides of silica (up to about 5%). This grade of titanium dioxide is likely to provide poorer water resistance in final coatings than the universal-grade titanium dioxide).


The voided latex particles useful herein have a particle size diameter of about 100 nm to about 2,500 nm and a void fraction of about 10% to about 75%. Preferably, the particles have a particle size of about 500 run to about 1,100 nm. The particles must have at least one void, but they may have multiple voids, non-spherical voids, interconnected voids, voids having channels connected to the outside of the particles, and they can encompass structures described as vesiculated and sponge-like. Preferably, the particles have a single void. They have a glass transition temperature (Tg), as measured by differential scanning calorimetry at a rate of 20° C./minute, of at least about 20° C., preferably at least about 50° C. The higher the Tg, the harder the particle is and the less likely it is to collapse. If the particles collapse, they are unable to contribute to hiding. The voided latex particles may be prepared by conventional polymerization processes known in the art, such as those disclosed in U.S. Pat. Nos. 3,784,391, 4,427,836; 4,469,825; 4,594,363; 4,798,691; 4,880,842; 4,908,271; 4,972,000; 5,041,464, 5,157,084; 5,216,044, 5,494,971; 5,545,695; and 6,020,435, as well as Japanese Patent Applications 60/223,873, 61/62510, 61/66710, 61/86941, 62/127336, 62/156387, 01/185311, and 02/140272.


Thickener


Suitable thickeners include both non-associative, water-soluble/water-swellable thickeners and associative thickeners. Suitable non-associative, water-soluble/water-swellable thickeners include polyvinyl alcohol (PVA), alkali soluble or alkali swellable emulsions known in the art as ASE emulsions, and cellulosic thickeners such as hydroxyalkyl celluloses including hydroxymethyl cellulose, hydroxyethyl cellulose and 2-hydroxypropyl cellulose, sodium carboxymethyl cellulose (SCMC), sodium carboxymethyl cellulose, 2-hydroxyethyl cellulose, 2-hydroxypropyl methyl cellulose, 2-hydroxyethyl methyl cellulose, 2-hydroxybutyl methyl cellulose, 2-hydroxyethyl ethyl cellulose, and the like. Suitable associative thickeners include hydrophobically-modified, alkali-soluble emulsions known in the art as HASE emulsions, hydrophobically-modified ethylene oxide-urethane polymers known in the art as HEUR thickeners, hydrophobically-modified cellulosics such as hydrophobically-modified hydroxyethyl cellulose, hydrophobically-modified polyacrylamides, and the like. Also useful as thickeners are fumed silica, attapulgite clay and other types of clay, titanate chelating agents, and the like.


Suitable dispersants include anionic polymers such as homopolymers and copolymers based on polycarboxylic acids, including those that have been hydrophobically- or hydrophilically-modified, e.g., polyacrylic acid, polymethacrylic acid, maleic anhydride and copolymers thereof with each other and with various monomers such as styrene, acrylate or methacrylate, diisobutylene, and other hydrophilic or hydrophobic comonomers. Suitable dispersants further include salts of the above dispersants and mixtures thereof.


The opacifying mixtures may include certain optional additives including defoamers, surfactants, coalescents, biocides, mildewcides, co-dispersants, dispersing resins, latex adsorbing resins, polymeric binders, and the voided latex polymers (described above).


Suitable defoamers include silicone-based and mineral oil-based defoamers and the like.


Suitable surfactants include cationic, anionic and non-ionic surfactants.


Suitable coalescents, plasticizers, and other optional solvents include ethylene glycol, propylene glycol, hexylene glycol, 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate (TEXANOL™), glycol ethers, mineral spirits, methyl carbitol, butyl carbitol, phthalates, adipates, and the like.


Suitable mildewcides and biocides include zinc oxide, isothiazolones, triazoles, and the like.


Suitable co-dispersants include non-ionic, anionic, and cationic dispersants such as 2-amino 2-methyl 1-propanol, dimethyl amino ethanol, potassium tripolyphosphate, trisodium polyphosphate, citric acid and other carboxylic acids, and the like.


Latex polymer binders are polymers or prepolymers which form the primary film of a paint. They bind the pigment and/or extenders, provide the required paint flow, and determine the gloss and hardness of the final paint film. The binder selected will depend upon the final use of the formulated paints. Binders suitable for exterior paints are generally suitable for interior paints, but binders suitable for interior paints may not be suitable for exterior paints. Suitable binders include, but are not limited to, homopolymers, copolymers, or terpolymers such as, for example, polyvinyl acetate, styrene-acrylic, styrene-butadiene, vinyl acetate-acrylic, ethylene-vinyl acetate, vinyl acetate-vinyl versatate, vinyl acetate-vinyl maleate, vinyl acetate-vinyl chloride-acrylic, ethylene-vinyl acetate-acrylic, and urethane polymers, optionally containing up to 10% by weight of functional groups (for example, but not limited to, carboxylic acid, phosphate, sulfate, sulfonate, amide and combinations thereof), other non-functional monomers, and mixtures thereof.







DETAILED DESCRIPTION OF THE INVENTION

All ranges disclosed herein are inclusive and the minimums and maximums of the nested ranges are combinable. All levels are in dry pounds/100 gallons i.e., pounds of solids/100 gallons of the mixtures unless otherwise noted. After the required ingredients and optional ingredients are combined, sufficient water is added to give a total of 100 gallons of the mixture.


The following optional ingredients may be included in any of the combination ranges shown below:












Optional Ingredients













Preferred

Preferred


Ingredient
Types
Types
Level
Level





Defoamer
any
solvent-
1-5
2-3




based,




silicone-




based


Surfactant
nonionic,
nonionic,
1-7
1-5



anionic, cationic
anionic


Solvent and
propylene glycol,
propylene
 1-200
 1-100


coalescent
ethylene glycol,
glycol,



hexylene glycol,
Texanol ®



2,2,4-trimethyl-1-3-



pentanediol



monoisobutyrate



(Texanol ®),



butyl carbitol,



methyl carbitol,



mineral spirits,


Base
ammonium
ammonium
up to 10
up to 5 



hydroxide,
hydroxide,



sodium hydroxide,
AMP-95



potassium



hydroxide,



2-amino 2-methyl



1-propanol (AMP)


Biocide
isothiazolones,
iso-
up to 5 
up to 3 



carbamates,
thiazolones



thiazoles,



phthalonitriles,



dioxanes,



hydantoins,



carbanilides,



triazines, ureas,



thiocyanates


Mildewcide
isothiazolones,
iso-
up to 20
up to 10



carbamates,
thiazolones



thiazoles,



phthalonitriles,



dioxanes,



hydantoins,



carbanilides,



triazines, ureas,



thiocyanates


Co-
2-amino 2-methyl
citric acid,
up to 5 
up to 2 


dispersant
1-propanol
KTTP, AMP



(AMP-95), dimethyl



amino ethanol



(DMEA), potassium



tripolyphosphate



(KTTP), trisodium



polyphosphate



(TSPP),


Polymeric
See above
vinyl acrylic,
 up to 150
up to 80


Binder
description
vinyl acetate,




styrene




acrylic


Voided latex
See above
x
 up to 100
up to 60


polymer
description










Combination No. 1


The combinations shown below do not require mixing to remain stable. They are exemplified in Example 1.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
MA/DIB,
MA/DIB
1.5-16 
3.7-14 


persant
BMA/MAA,



AA/HPA, SMA


Thick-
HEUR effective
HEUR
0.2-20 
10-16


ener
hydrophobe
effective



C4-C12 MW
hydrophobe



10,000-200,000,
C4-C12 and




MW 12,000-




150,000



HEUR effective
HEUR
0.8-5  
0.2-2  



hydrophobe
effective



C6-C30 MW
hydrophobe



10,000-200,000,
C6-C24 and



or combinations
MW 12,000-



thereof
150,000


TiO2
Universal grade
Universal TiO2
 600-1500
 700-1400



coated with
coated with



1%-7% Al2O3,
1.5-5% Al2O3



up to 15% SiO2
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 2


The following combinations do not require mixing to remain stable. They are exemplified in Example 2.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
MA/DIB,
PAA
1.8-23 
 3.5-16.8


persant
BMA/MAA,



AA/HPA, PAA


Thick-
HASE effective
HASE effective
0.3-5  
1-3


ener
hydrophobe
hydrophobe



C6-C22 MW
C6-C18 and



10,000-7,000,000
MW 100,000-




5,000,000


TiO2
Interior grade
Interior grade
 600-1500
 700-1400



coated with
coated with



1-7% Al2O3/
2-5% Al2O3/



0-5% SiO2 0-5%
0-3% SiO2










Combination No. 3


The following combinations do not require mixing to remain stable. They are exemplified in Example 3.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
PAA
PAA
1.8-23 
 3.5-16.8


persant


Thick-
Hydroxy-
Hydroxyethyl
0.5-3  
1-2


ener
alkylcellulose and
cellulose



combinations
MW 100,000-



thereof MW
2,000,000



10,000-



10,000,000


TiO2
Interior grade
Interior grade
 600-1500
 700-1400



coated with
coated with



1-7% Al2O3
2-5% Al2O3/



up to 5% SiO2
up to 3% SiO2










Combination No. 4


The following combinations do not require mixing to remain stable. They are exemplified in Example 4.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
PAA
PAA
1.8-23 
 3.5-16.8


persant


Thick-
Hydrophobically-
Hydro-
2-6
3-5


ener
modified
phobically-



hydroxy-
modified



alkyllcellulose
hydroxy-



MW 10,000-
ethylcellulose



10,000,000
MW 50,000-




2,000,000


TiO2
Universal coated
Universal
 600-1500
 700-1400



with 1-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 5


The following combinations do not require mixing to remain stable. They are exemplified in Example 5.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
MA/DIB or
MA/DIB or
 3.0-22.5
 5.6-16.8


persant
AA/HPA
AA/HPA
MA/DIB
MA/DIB





 0.5-22.5
2.8-14 





AA/HPA
AA/HPA


Thick-
Hydrophobically-
Hydro-
0.2-10 
0.5-5  


ener
modified
phobically-



hydroxyalkyl
modified



cellulose
hydroxyethyl



MW 10,000-
cellulose



10,000,000
MW 50,000-




2,000,000


Thick-
HEUR effective
HEUR
 2-10
 5-10


ener
hydrophobe
effective



C4-C30
hydrophobe



MW 10,000-
C6-C24



200,000
MW 12,000-




150,000


TiO2
Universal coated
Universal
 600-1500
 700-1400



with 1-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 6


The following combinations requires occasional mixing to remain stable. They are exemplified in Example 6.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
AA/HPA
AA/HPA
0.5-22.5
2.8-14  


persant


Thick-
Hydrophobically-
Hydro-
1-10
2-7 


ener
modified
phobically-



hydroxyalkyl
modified



cellulose
hydroxyethyl



MW 10,000-
cellulose



1,000,000
MW 50,000-



or
1,000,000



Hydroxyethyl
Hydroxyethyl
1-10
2-7 



cellulose
cellulose



MW 10,000-
MW 100,000-



1,000,000
1,000,000



or



combinations of



the above



or



combinations of

2-12
4-10



the above



with:



HEUR effective
HEUR
2-12
3-6 



hydrophobe
effective



C4-C30
hydrophobe



MW 10,000-
C6-C24



200,000
MW 12,000-



or
150,000



attapulgite clay


TiO2
Universal coated
Universal
600-1500
700-1400



with 1.0-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 7


The following combinations requires occasional mixing to remain stable. They are exemplified in Example 7.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
PAA
PAA
1.2-45 
3.5-28 


persant


Thick-
HASE effective
HASE effective
0.3-5  
1.0-3  


ener
hydrophobe
hydrophobe



C6-C22
C6-C18



MW 10,000-
MW 100,000-



7,000,000
5,000,000


TiO2
Universal coated
Universal
 600-1500
 700-1400



with 1-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 8


The following combinations requires constant mixing to remain stable. They are exemplified in Example 8.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
MA-DIB
MA-DIB
1.2-18 
3.5-14 


persant


Thick-
Hydrophobically-
Hydro-
0.5-10 
0.5-8  


ener
modified
phobically-



hydroxyalkyl
modified



cellulose
hydroxyethyl



MW 10,000-
cellulose



1,000,000
MW 50,000-



or
1,000,000



Hydroxyethyl
Hydroxyethyl



cellulose
cellulose



MW 10,000-
MW 100,000-



1,000,000
1,000,000



or



combinations of



the above


TiO2
Universal coated
Universal
 600-1500
 700-1400



with 1-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 9


The following combinations requires constant mixing to remain stable.
















Ingre-

Preferred

Preferred


dients
Types
Types
Level
Level







Dis-
AA/HPA
AA/HPA
 0.6-22.5
2.8-14 


persant


Thick-
HASE effective
HASE effective
0.1-3  
0.3-2  


ener
hydrophobe
hydrophobe



C6-C22
C6-C18



MW 10,000-
MW 100,000-



7,000,000
5,000,000


TiO2
Universal coated
Universal
 600-1500
 700-1400



with 1-7%
coated with



Al2O3,
1.5-5% Al2O3,



up to 15% SiO2,
1.2-12% SiO2,



up to 15% ZrO2
up to 4% ZrO2










Combination No. 10


The following combinations will require constant mixing to remain stable.
















Ingred-

Preferred

Preferred


ients
Types
Types
Level
Level







Dispersant
MA/DIB
MA/DIB
0.6-45 
2.8-21 


Thickener
HASE effective
HASE effective
0.1-3  
0.3-2  



hydrophobe
hydrophobe



C6-C22 MW
C6-C18 MW



10,000-
100,000-



7,000,000
5,000,000


TiO2
Universal coat-
Universal coat-
 600-1500
 700-1400



ed with 1-7%
ed with 1.5-5%



Al2O3, up to
Al2O3,



15% SiO2, up
1.2-12% SiO2,



to 15% ZrO2
up to 4% ZrO2










Combination No. 11


The following combinations require constant mixing to remain stable.
















Ingred-

Preferred

Preferred


ients
Types
Types
Level
Level







Dispersant
MA/DIB
MA/DIB
1.2-18 
3.5-14 


Thickener
HEUR effec-
HEUR effec-
0.2-20 
10-16



tive hydro-
tive hydro-



phobe C4-C12
phobe C4-C12



MW 10,000-
MW 12,000-



200,000 or
150,000



HEUR effec-
HEUR effec-
0.8-5  
0.2-2  



tive hydro-
tive hydro-



phobe C6-C30
phobe C6-C24



average MW
MW 12,000-



10,000-
150,000



200,000 or



combinations



thereof


TiO2
Interior grade
Interior grade
 600-1500
 700-1400



coated with
coated with



1-7% Al2O3,
2-5% Al2O3,



up to 5% SiO2
up to 3% SiO2









Test Procedures

The Stormer viscosity of the mixtures is measured using ASTM method D562.


The Brookfield viscosity of the mixtures is measured using spindle #4 of a Brookfield viscometer at 6 rpm.


The ICI viscosity of the mixtures is measured using ASTM method D3205-77.


In the following examples, the mixtures may be prepared using a laboratory mixer having a 45° pitch stirring blade. The water and optional dispersant, defoamer, surfactant and/or biocide are combined and mixed. The titanium dioxide slurry is slowly added and the mixture is stirred for 15-20 minutes. The binder and optional coalescent, rheology modifier, ammonia, and additional water, if necessary, are then added.


In the above description and in the examples, the following abbreviations are used:












Abbreviations
















AA
Acrylic acid


PAA
Polyacrylic acid


MA/DIB
Maleic acid/diisobutylene copolymer


AA/HPA
Acrylic acid/hydroxypropyl acid


BMA/MAA
Butylmethacrylate/methacrylic acid copolymer


SMA
Styrene or alpha methylstyrene/alkylacrylate (optional)/



methacrylic or acrylic acid copolymers or terpolymers


HEC
Hydroxyethyl cellulose


HMHEC
Hydrophobically-modified HEC


HEUR
Hydrophobically-modified ethylene oxide-based urethane



block copolymers


HASE
Hydrophically-modified alkali soluble emulsions


TiO2
Titanium dioxide


Al2O3
Alumina or oxide of aluminum


SiO2
Silica or oxide of silicon


ZrO2
Zirconium dioxide


cps
centipoises


MW
molecular weight as measured by gel permeation



chromatography









EXAMPLES
Example 1

Mixtures A to E described below will require no mixing to remain stable.



















A



Ingredients
lbs/100 gallons














Grind prepared on




Cowles disperser



Water
258.35



Propylene glycol
50



Tamol ™ 731 MA/DIB
53.42



dispersant



Foamaster ® VL defoamer
1.50



Triton CF-10 surfactant
2.00



Kathon ® LX 1.5%
2.00



biocide



Ti-Pure ® R706 universal-
1335.56



grade TiO2



Letdown prepared on



Cowles disperser



Ammonia hydroxide
0.6



(28%)



Foamaster ® VL defoamer
1.50



Acrysol ® RM-2020NPR
30.00



HEUR thickener



Letdown (on low speed



mixer)



Acrysol ® RM-2020NPR
40.40



HEUR thickener



Water
68.96



KU initially after
90



preparation



pH initially after
9.20



preparation



ICI initially after
2.8



preparation



Brookfield viscosity
2500



(cps at 1.25 sec−1)



Actual scale prepared
50



(gallons)
















B
C
D
E



lbs/100
lbs/100
lbs/100
lbs/100


Ingredients
gallons
gallons
gallons
gallons














Grind prepared on






Cowles disperser


Water
130
130
130
130


Propylene glycol
50
50
50
50


Tamol ® 731 MA/DIB
29.38
29.38
29.38
29.38


dispersant


Foamaster ® VL
3.00
3.00
3.00
3.00


defoamer


Triton CF-10 surfactant
2.00
2.00
2.00
2.00


Kathon ® LX 1.5%
2.00
2.00
2.00
2.00


biocide


Ti-Pure ® R-706
734.56
734.56
734.56
734.56


universal-grade TiO2


Rhoplex ® SG-10M
151.20
151.20
151.20
151.20


acrylic binder


Texanol ® coalescent
12.5
12.5
12.5
12.5


Ammonium hydroxide
0.60
0.60
0.60
0.60


(28%)


Ropaque ® Ultra opaque
164.44
164.44
164.44
164.44


polymer


Acrysol ® RM-
30
30
30
30


2020NPR HEUR


thickener


Letdown prepared on low


speed mixer)


Co-thickener type
Acrysol ®
Acrysol ®
Acrysol ®
Acrysol ®



RM-
RM-825
SCT-275
RM-12W



2020NPR
HEUR
HEUR
HEUR



HEUR


Level of co-thickener
33.5
2.24
2.63
4.84


water
60.0
91.2
90.8
88.5


KU initially after
93
99
96
96


preparation


pH initially after
8.80
8.78
8.76
8.74


preparation


ICI initially after
3.0
1.7
1.8
1 7


preparation


Brookfield viscosity
3010
3710
6010
24000


(cps at 1.25 sec−1)


Actual scale prepared
50
50
50
50


(gallons)









Example 2

Mixtures A to G described below will require no mixing to remain stable.



















A
B
C
D



lbs/100
lbs/100
lbs/100
lbs/100


Ingredients
gallons
gallons
gallons
gallons














Grind prepared on






Cowles disperser


Water
228.00
228.00
228.00
228.00


Propylene glycol
50.00
50.00
50.00
50.00


Tamol ® 1254
38.16
38.16
38.16
38 16


AA/MAA dispersant


Triton ® CF-10
2.00
2.00
2.00
2.00


surfactant


Foamaster ® VL
1.50
1.50
1.50
1.50


defoamer


Kathon ® LX 1.5%
2.00
2.00
2.00
2.00


biocide


Ti-Pure ® R900 interior-
1335.52
1335.52
1335.52
1335.52


grade TiO2


Letdown prepared on


Cowles disperser


Foamaster ® VL
1.50
1.50
1.50
1.50


defoamer


Water
97.00
97.00
97.00
97.00


Ammonium hydroxide
0.4
0.4
0.4
0.4


(28%)


Acrysol ® DR-1 HASE
1.0
1.0
1.0
1.0


thickener


Letdown prepared on low


speed mixer


Acrysol ® DR-1 HASE
4.0
5.0
6.0
7.0


thickener


Water
83.96
82.96
81.96
80.96


KU initially after
77
80
83
87


preparation


pH initially after
0.4
0.5
0.6
0.6


preparation


ICI initially after
9.06
8.98
8.89
8.79


preparation


Brookfield viscosity
12800
14500
15000
16700


(cps at 1.25 sec−1)


Actual scale prepared
50
50
50
50


(gallons)














E
F
G



lbs/100 gallons
lbs/100 gallons
lbs/100 gallons














Grind prepared on





Cowles disperser


Water
228.00
228.00
228.00


Propylene glycol
50.00
50.00
50.00


Tamol ® 1254
38.16
38.16
38.16


AA/MAA dispersant


Triton ® CF-10
2.00
2.00
2.00


surfactant


Foamaster ® VL
1.50
1.50
1.50


defoamer


Kathon ® LX 1.5%
2.00
2.00
2.00


biocide


Ti-Pure ® R900 in-
1335.52
1335.52
1335.52


terior grade TiO2


Letdown prepared on


Cowles disperser


Foamaster ® VL
1.50
1.50
1.50


defoamer


Water
97.00
97.00
97.00


Letdown prepared on


low speed mixer


Thickener type
Acrysol ® DR-
Acrysol ® DR-
Acrysol ® DR-



73 HASE
1 HASE
3 HASE


Level of thickener
6.86
6.08
6.04


Ammonia hydroxide
0.40
0.30
0.22


(28%)


Water
82.08
82.96
83.08


KU initially after
81
81
81


preparation


pH initially after
0.8
0.6
0.7


preparation


ICI initially after
9.01
8.96
8.99


preparation


Brookfield viscosity
15700
15300
15200


(cps at 1.25 sec−1)


Actual scale prepared
50
50
50


(gallons)









Example 3

Mixture A described below will require no mixing to remain stable.

















A



Ingredients
lbs/100 gallons



















Grind prepared on Cowles disperser




Water
228.00



Propylene glycol
50.00



Tamol ® 1254 AA/MAA dispersant
38.16



Triton ® CF-10 surfactant
2.00



Foamaster ® VL defoamer
1.50



Kathon ® LX 1.5% biocide
2.00



Ti-Pure ® R900 interior-grade TiO2
1335.52



Letdown prepared of Cowles disperser



Foamaster ® VL defoamer
1.50



Water
97.00



Letdown prepared on low speed mixer



Natrosol ® 250 MHR (3.5% solution in
41.16



water) HEC thickener



Water
48.18



KU initially after preparation
80



pH initially after preparation
0.6



ICI initially after preparation
9.37



Brookfield viscosity
15100



(cps at 1.25 sec−1)



Actual scale prepared (gallons)
50










Example 4

Mixture A described below will require no mixing to remain stable.

















A



Ingredients
lbs/100 gallons



















Grind prepared on Cowles disperser




Water
168.76



Propylene glycol
62.5



Tamol ® 1254 AA/MAA dispersant
26.24



Foamaster ® VL defoamer
1.88



Triton ® CF-10 surfactant
2.50



Kathon ® LX 1.5% biocide
2.50



Ti-Pure ® R902 universal-grade TiO2
918.2



Letdown prepared on Cowles disperser



Foamaster ® VL defoamer
1.88



Ropaque ® Ultra opaque polymer
205.56



Letdown prepared on a low speed mixer



Natrosol ® Plus 430 (4% in solution in
89.52



water) HMHEC thickener



Ammonia hydroxide (28%)
0.46



Water
55.46



KU initially after preparation
97



pH initially after preparation
8.77



ICI initially after preparation
1.0



Brookfield viscosity
18000



(cps at 1.25 sec−1)



Actual scale prepared (gallons)
50










Example 5

Mixtures A to C described below will require no mixing to remain stable.



















A



Ingredients
lbs/100 gallons














Grind prepared on Cowles disperser




Water
160



Propylene glycol
50



Tamol ® 1124 AA/HPA dispersant
7.35



Kathon ® LX 1.5% biocide
2.00



Ti-Pure ® R706 universal-grade TiO2
918.2



Letdown prepared on Cowles disperser



Foamaster ® VL defoamer
1.5



Ropaque ® Ultra opaque polymer
205.56



Acrysol ® RM-2020NPR HEUR
40.0



thickener



Natrosol ® Plus 330 (3% in solution in
68.32



water) HMHEC thickener



Ammonium hydroxide (28%)
2.16



Water
76.3



KU initially after preparation
98



pH initially after preparation
8.73



ICI initially after preparation
1.3



Brookfield viscosity
18500



(cps at 1.25 sec−1)



Actual scale prepared (gallons)
50















B



Ingredients
lbs/100 gallons














Grind prepared on Cowles disperser




Water
130



Propylene glycol
50



Tamol ® 731 MA/DIB dispersant
29.38



Foamaster ® VL defoamer
1.50



Triton ® CF-10 surfactant
2.00



Kathon ® LX 1.5% biocide
2.00



Ti-Pure ® R706 universal-grade TiO2
734.56



Letdown prepared on Cowles disperser



Rhoplex ® SG-10M acrylic binder
151.20



Texanol ® coalescent
12.5



Ammonium hydroxide (28%)
0.60



Ropaque ® Ultra opaque polymer
164.44



Foamaster ® VL defoamer
1.50



Acrysol ® RM-2020NPR HEUR
30.00



thickener



Letdown prepared on low speed mixer



Natrosol ® Plus 330 (3% in solution in
27.6



water) HMHEC thickener



Water
65.82



KU initially after preparation
98



pH initially after preparation
8.73



ICI initially after preparation
1.9



Brookfield viscosity
10800



(cps at 1.25 sec−1)



Actual scale prepared (gallons)
50















C



Ingredients
lbs/100 gallons














Grind prepared on Cowles disperser




Water
130



Propylene glycol
50



Tamol ® 731 MA/DIB dispersant
30.04



Foamaster ® VL defoamer
1.50



Triton ® CF-10 surfactant
2.00



Kathon ® LX 1.5% biocide
2.00



Kronos ® 2102 universal-grade TiO2
751.09



Rhoplex ® SG-10M acrylic binder
151.2



Texanol ® coalescent
12.49



Ammonia hydroxide (28%)
0.60



Ropaque ® Ultra opaque polymer
164.44



Foamaster ® VL defoamer
1.50



Acrysol ® RM-2020NPR HEUR
30.00



thickener



Letdown prepared on low speed mixer



Natrosol ® Plus 330 (3% in solution in
25.04



water) HMHEC thickener



Water
67.76



KU initially after preparation
99



pH initially after preparation
1.8



ICI initially after preparation
9.22



Brookfield viscosity
10100



(cps at 1.25 sec−1)



Actual scale repared (gallons)
50










Example 6

Mixtures A to D described below will require occasional mixing to remain stable.

















A
B


Ingredients
lbs/100 gallons
lbs/100 gal












Grind prepared on Cowles disperser




Water
272.7
272.7


Tamol ® 1124 AA/HPA dispersant
7.35
7.35


Kathon ® LX 1.5% biocide
2.00
2.00


Ti-Pure ® R706 universal-grade TiO2
918.2
918.2


Letdown prepared on low speed mixer


Triton ® CF-10 surfactant
0
1.0


Propylene glycol
50
50


Foamaster ® VL defoamer
1.5
1.5


Ropaque ® Ultra opaque polymer
205.56
205.56


Natrosol ® Plus 330 (3% in solution in
192
113


water) HMHEC thickener


Attagel ® 50 attagulpite clay (100%

5.0


solid)


Ammonia hydroxide (28%)
1.96
1.98


KU initially after preparation
92
94


pH initially after preparation
0.5
0.5


ICI initially after preparation
8.87
8.75


Brookfield viscosity
23000
27700


(cps at 1.25 sec−1)


Actual scale prepared (gallons)
57
53













C
D


Ingredients
lbs/100 gallons
lbs/100 gallons












Grind prepared on Cowles disperser




Propylene glycol
50
50


Water
160
160


Tamol ® 1124 AA/HPA dispersant
7.35
7.35


Kathon ® LX 1.5% biocide
2.00
2.00


Ti-Pure ® R706 universal-grade TiO2
918.2
918.2


Letdown prepared on low speed mixer


Foamaster ® VL defoamer
1.5
1.5


Ropaque ® Ultra opaque polymer
205.56
205.56


Natrosol ® Plus 330 (3% in solution in
80.06


water) HMHEC thickener


Natrosol ® 250 MHR (3.5% in solution

134.7


in water) HEC thickener


Ammonium hydroxide (28%)
1.80
1.86


Water
106.7
50.22


KU initially after preparation
94
98


pH initially after preparation
8.68
8.67


ICI initially after preparation
0.5
0.8


Brookfield viscosity
18700
28200


(cps at 1.25 sec−1)


Actual scale prepared (gallons)
50
50









Example 7

Mixtures A to E described below will require occasional mixing to remain stable.


















A
B
C
D
E



lbs/100
lbs/100
lbs/100
lbs/100
lbs/100


Ingredients
gallons
gallons
gallons
gallons
gallons




















Grind pre-







pared on


Cowles dis-


perser


Water
115
115
115
115
93.46


Propylene
50
50
50
50
40.64


glycol


Tamol ®
20.99
10.49
31.48
41.97
25 59


1254 AA/


MAA


dispersant


Foamaster ®
2.00
2.00
2.00
2.00
2.44


VL defoamer


Triton ®
1.50
1.50
1.50
1.50
1.63


CF-10


surfactant


Kathon ®
2.00
2.00
2.00
2.00
1.63


LX 1.5%


biocide


Ti-Pure ®
734.56
734.56
734.56
734.56
596.96


R706 univer-


sal-grade


TiO2


Foamaster ®
1.50
1.50
1.50
1.50


VL defoamer


Ropaque ®
164.44
164.44
164.44
164.44
133.64


Ultra opaque


polymer


Letdown


prepared on


low speed


mixer


Res 3083
140.10
140.10
140.10
140.10
245.05


emulsion


Texanol ®
11.37
11.37
11.37
11.37
15.73


coalescent


Acrysol ®
9.6
7.12
5.67
4.12
7.92


DR-3 HASE


thickener


Ammonium
2.12
2.34
1.96
1.81
2.28


hydroxide


(28%)


Water
150.8
152.8
145.55
138.67
144.93


KU initially
100
101
99
97
98


after


preparation


pH initially

8.69
8.54
8.68
8.4


after


preparation


ICI initially
0.9
0.8
0.8
0.7
1.1


after


preparation


Brookfield
27700
29200
31600
29900
23800


viscosity


(cps at 1.25


sec−1)









Example 8

Mixtures A and B described below will require constant mixing to remain stable.


















A
B




lbs/100
lbs/100



Ingredients
gallons
gallons









Grind prepared on Cowles disperser





Water
174.98
174.98



Propylene glycol
62.49
62.49



Tamol ® 731 MA/DIB dispersant
36.72
36.72



Foamaster ® VL defoamer
1.87
1.87



Triton ® CF-10 surfactant
2.50
2.50



Kathon ® LX 1.5% biocide
2.50
2.50



Ti-Pure ® R706 universal-grade TiO2
918.12
918.12



Letdown prepared on Cowles disperser



Foamaster ® VL defoamer
1.87
1.87



Ropaque ® Ultra opaque polymer
205.53
205.53



Letdown on a low speed mixer



Natrosol ® Plus 330 (3% in solution in

45.09



water) HMHEC thickener



Natrosol ® 250 MHR (3.5% in solution
127.69
45.09



in water) HEC thickener



Ammonium hydroxide (28%)
1.00
1.34



Water
0
80.99



KU initially after preparation
99
99



pH initially after preparation
8.69
8.76



ICI initially after preparation
1.6
0.8



Brookfield viscosity
20200
22700



(cps at 1.25 sec−1)



Actual scale prepared (gallons)
100
100




















Supplier Information









Material Name
Description
Supplier





Tamol ™ 1124
Dispersant
Rohm and Haas Company




(Philadelphia, PA)


Tamol ™ 1254
Dispersant
Rohm and Haas Company




(Philadelphia, PA)


Tamol ™ 731
MA/GIB Dispersant
Rohm and Haas Company




(Philadelphia, PA)


Acrysol ™ DR-1
HASE Thickener
Rohm and Haas Company




(Philadelphia, PA)


Acrysol ™ DR-3
HASE
Rohm and Haas Company



Thickener/Rheology
(Philadelphia, PA)



Modifier


Acrysol ™ DR-73
HASE Thickener
Rohm and Haas Company




(Philadelphia, PA)


Acrysol ™ RM-2020
HEUR
Rohm and Haas Company


NPR
Thickener/Rheology
(Philadelphia, PA)



Modifier


Rhoplex ™ SG-10M
Emulsion Polymer
Rohm and Haas Company



Binder
(Philadelphia, PA)


RES 3083
Emulsion Polymer
Rohm and Haas Company



Binder
(Philadelphia, PA)


Kathon ™ LX 1.5%
Biocide
Rohm and Haas Company




(Philadelphia, PA)


Triton ™ CF-10
Surfactant
Union Carbide Corporation




(Danbury, CT)


Foamaster ™ VL
Defoamer
Henkel Corporation (King




of Prussia, PA)


Ti-Pure ™ R-706
Titanium Dioxide
E. I. Dupont de Nemours




and Co., Inc.




(Wilmington, DE)


Ti-Pure ™ R-900
Titanium Dioxide
E. I. Dupont de Nemours




and Co., Inc.




(Wilmington, DE)


Ti-Pure ™ R-902
Titanium Dioxide
E. I. Dupont de Nemours




and Co., Inc.




(Wilmington, DE)


Kronas ® 2102
Universal Grade
Kronas (Houston, TX)



Titanium Dioxide


Ropaque ®
Ultra Opaque
Rohm and Haas



Synthetic/Polymer
(Philadelphia, PA)


Texanol ™
Coalescent
Eastman Chemical




(Kings Port, TN)


Natrosol ®
HEC Thickner
Hercules (Wilmington, DE)


Natrosol ® Plus 430
HMHEC Thickener
Hercules (Wilmington, DE)


Natrosol ® Plus 330
HMHEC Thickener
Hercules (Wilmington, DE)


Natrosol ® 250 MHR
HEC Thickener
Hercules (Wilmington, DE)


Attrgel ® 50
Attapulgite Clay
Engelhardt (Edison, NJ)








Claims
  • 1. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.2 to about 20 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener selected from the group consisting of: (i) a HEUR having a C4-C12 hydrophobe and a molecular weight of about 10,000 to about 200,000, (ii) a HEUR having a C6-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000, and (iii) combinations thereof, (c) about 1.5 to about 16 lbs/100 gallons of at least one dispersant selected from the group consisting of a maleic acid/diisobutylene copolymer, a butyl methacrylate/methacrylic acid copolymer, and an acrylic acid/hydroxypropyl acrylate copolymer; and (d) water.
  • 2. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of to about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one interior-grade titanium dioxide; (b) about 0.3 to about 5 lbs/100 gallons of at least one hydrophobically modified, alkali-soluble emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; (c) about 1.8 to about 23 lbs/100 gallons of at least one dispersant selected from the group consisting of a maleic acid/diisobutylene copolymer, a butyl methacrylate/methacrylic acid copolymer, an acrylic acid/hydroxypropyl acrylate copolymer and a polyacrylic acid; and (d) water.
  • 3. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 2 to about 6 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; (c) about 1.8 to about 23 lbs/100 gallons of at least one polyacrylic acid dispersant; and (d) water.
  • 4. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.2 to about 10 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; (c) about 2 to about 10 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000; (d) about 3.0 to about 22.5 lbs/100 gallons of at least one maleic acid/diisobutylene copolymer dispersant; and (e) water.
  • 5. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.2 to about 10 lbs/100 gallons of at least one hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; (c) about 2 to about 10 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000, (d) about 0.5 to about 22.5 lbs/100 gallons of at least one acrylic acid/hydroxypropyl acrylate dispersant; and (e) water.
  • 6. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.2 to about 10 lbs/100 gallons of at least one hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,0000 or a hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; (c) about 0.5 to about 22.5 lbs/100 gallons of at least one acrylic acid/hydroxypropyl acrylate dispersant; and (d) water.
  • 7. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.3 to about 5 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and molecular weight of about 10,000 to about 7,000,000; (c) about 1.2 to about 45 lbs/100 gallons of at least one polyacrylic acid dispersant; and (d) water.
  • 8. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.5 to about 10 lbs/100 gallons of a hydrophobically-modified hydroxyalkyl cellulose thickener having a molecular weight of about 10,000 to about 10,000,000; (c) about 1.2 to about 18 lbs/100 gallons of at least one maleic acid/diisobutylene dispersant; and (d) water.
  • 9. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.1 to about 3 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; (c) about 0.6 to about 22.5 lbs/100 gallons of at least one acrylic acid—hydroxypropyl acrylate dispersant; and (d) water.
  • 10. A fluid opacifying pigment mixture having a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one universal-grade titanium dioxide; (b) about 0.1 to about 3 lbs/100 gallons of at least one hydrophobically-modified, alkali-soluble or alkali-swellable emulsion (HASE) thickener having a C6-C22 hydrophobe and a molecular weight of about 10,000 to about 7,000,000; (c) about 0.6 to about 45 lbs/100 gallons of at least one maleic acid/diisobutylene copolymer dispersant; and (d) water.
  • 11. A fluid opacifying pigment mixture, a titanium dioxide pigment volume concentration of about 40 to about 100%, a titanium having dioxide volume solids content of at least about 15%, and a Stormer viscosity of about 50 to about 250 KU, which mixture comprises: (a) about 600 to about 1500 lbs/100 gallons of at least one interior-grade titanium dioxide; (b) about 0.2 to about 20 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener selected from the group consisting of a HEUR having a C4-C12 hydrophobe and a molecular weight of about 10,000 to about 200,000, a HEUR having a C6-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000, and combinations thereof; (c) about 1.2 to about 18 lbs/100 gallons of at least one maleic acid/diisobutylene dispersant; and (d) water.
  • 12. The mixture of claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, or 11, which further comprises one or more additives selected from the group consisting of a defoamer, a surfactant, a coalescent, a base, a biocide, a mildewcide, a co-dispersant, a polymeric binder, and a voided latex polymer.
  • 13. The mixture of claim 6, further comprising about 2 to about 12 lbs/100 gallons of at least one hydrophobically-modified ethylene oxide-urethane polymer (HEUR) thickener having a C4-C30 hydrophobe and a molecular weight of about 10,000 to about 200,000 or at least one clay thickener.
  • 14. The mixture of claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, or 12, wherein the pigment volume concentration is about 50 to 100%.
  • 15. The mixture of claim 14, wherein the pigment volume concentration is about 60 to about 100%.
  • 16. The mixture of claim 15, wherein the pigment volume concentration is about 70 to about 100%.
  • 17. The mixture of claim 16, wherein the pigment volume concentration is about 80 to about 100%.
  • 18. The mixture of claim 17, wherein the pigment volume concentration is about 90 to about 100%.
  • 19. The mixture of claims 6-11, wherein said mixing is carried out using an impeller, a recirculator, a shaker, a mill, a rotator, a bubbler, a sonicator, a pump or combinatiuons thereof.
CROSS REFERENCE TO RELATED APPLICATIONS

This application claims priority to U.S. Provisional Applications Ser. No. 60/183,655 filed Feb. 18, 2000, Ser. No. 60/183,656 filed Feb. 18, 2000, and Ser. No. 60/247,639 filed Nov. 10, 2000.

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Related Publications (1)
Number Date Country
20020002934 A1 Jan 2002 US
Provisional Applications (3)
Number Date Country
60183655 Feb 2000 US
60183656 Feb 2000 US
60247639 Nov 2000 US