Stable calcined clay slurries

Abstract: A stabilized aqueous calcined clay slurry and a method for preparing the same are provided. The method involves preparing an aqueous slurry of calcined clay containing at least 10% by weight calcined clay, and 0.05% to 1.0% by weight of anionic emulsion copolymer.

Description: The present invention is concerned with stable clay slurries and particularly to slurries of calcined kaolin clay. More particularly, the present invention is concerned with the use of crosslinked or uncrosslinked acid-containing, alkali-soluble acrylic copolymers, or combinations thereof, to achieve stable calcined kaolin slurries such that said slurries can be shipped and/or stored without the harmful effects of dilatant settling. Kaolin, a naturally occurring form of hydrated aluminum oxide commonly known as hydrated clay, is widely used in paper coatings, as a filler in paper manufacture, as a paint additive, and in coatings for wire and cable. For many applications, the kaolin clay must first be calcined in order to take on certain desirable characteristics. Raw kaolin or aqueous kaolin slurries are calcined, i.e. brought to an elevated temperature, such that the clay loses its water of hydration and becomes a powdered solid. It is the calcined kaolin which has the desirable properties of increasing the whiteness and raising the level of opacity of materials coated with it. Calcined kaolin clay retains its desirable properties even after it is reslurried. Since calcined kaolin is used in large quantities as an aqueous slurry, it is desirable to be able to ship it as a high solids aqueous slurry. Unfortunately, these slurries are fairly unstable. Calcined clay particles have a highly irregular shape which is responsible for their property of increasing opacity. However, this irregular shape is also a major cause of calcined day slurry instability. As a calcined clay slurry is agitated, the irregularly shaped particles sweep out an abnormally large volume, thereby increasing the statistical likelihood of particles colliding, forming agglomerates and settling out. This is known as dilatant settling. Dilatant settling and slurry instability result in the formation of hard-pack solids precipitation. This hard-pack renders the slurry useless as an article of commerce and potentially damaging to piping, pumps, and other slurry handling mechanical equipment. The large volume swept out by the particles also dramatically increases the high shear viscosity of calcined clay slurries. This high shear viscosity, characteristic of calcined clay slurries, presents major handling problems for the industry because the calcined clay slurries are applied to substrates under high shear conditions. In order to prevent the effects of dilatancy on slurry viscosity and slurry stability, the level of solids of a calcined kaolin clay slurry must be kept low (40 to 50% by weight) relative to non-calcined clay slurries which can have levels of clay solids of about 70% by weight. These problems have been the subject of extensive research and have been long standing problems for the calcined clay industry. U.S.-A-4,017,324 teaches the use of 8 to 33.5% hydrated kaolin clay along with a suspending agent, such as bentonite clay, hydroxyethyl cellulose, methyl cellulose, or carboxymethyl cellulose, and a dispersing agent such as a non-ionic surfactant, an anionic surfactant, an alkanolamine or the sodium salt of a polymeric carboxylic acid. U.S.-A-4,374,203 discloses the use of anionic polymers and copolymers in combination with cationic polymers as a means of controlling calcined clay slurry viscosity and stability. The examples contained in that patent which use only an anionic copolymer do not show any advantage with regard to decreasing the dilatancy of the slurries. The approaches of these U.S. patents are only somewhat effective in solving the problems of calcined kaolin clay slurry stability and dilatancy. Also, since these methods involve the use of two or more compounds to achieve stable slurries, they present manufacturing difficulties and increased costs. In addition, dilatant settling may still occur, resulting in unusable slurries. US 3846147 discloses a calcined clay pigment suspension containing 1.34% by weight of an anionic copolymer. It teaches that a pH of at least 8 is required for stabilising of the suspension. We have now found a method for preparing calcined clay slurries which enable the problems mentioned above to be solved. Stable calcined clay slurries can be made containing at least 10% by weight calcined clay solids by adding to said slurries an effective amount of anionic, acrylic emulsion copolymer. The present invention enables the preparation of stable aqueous slurries of clay, especially calcined kaolin clay, which do not exhibit dilatant settling even after prolonged storage without agitation, and which can be pumped without suffering the effects of dilatancy. According to the present invention there is provided a stable calcined clay slurry, which comprises at least 10% by weight of calcined clay in an aqueous medium in the presence of 0.05% to 1.0% by weight, based on the total weight of solids, of anionic emulsion copolymer having an acid equivalent weight of solids value, determined by dividing the formula weight of the acid component by the relative amount of that component in the copolymer, of less than 200 wherein the anionic emulsion copolymer comprises from 30% to 60% by weight of the total polymer concentration of polymerized monomeric units of unsaturated non carboxylic acids and from 40% to 70% by weight of the total polymer concentration of polymerized monomeric units of monoethylenically unsaturated monocarboxylic acid. This invention is directed to the use of an acid-containing, high charge density, alkali-soluble, anionic copolymer as a clay slurry stabilizer. The slurry may, for example, be in the form of a suspension or a dispersion. The present invention also provides a process of making a stable calcined clay slurry of the invention, which comprises:- (a) (i) when the slurry is to be formed as a suspension, dissolving in water the anionic emulsion copolymer; or (ii) when the slurry is to be formed as a dispersion, dissolving in water the anionic emulsion copolymer and, optionally, dispersing agent; (b) adding at least 10% by weight of calcined clay to the solution obtained in (a)(i) to provide a suspension, or to the solution obtained in (a)(ii) to provide a dispersion; and (c) adjusting the pH of the suspension or dispersion to a pH of about 6 to about 8. We have found that the use of high charge density, acid-containing, alkali-soluble copolymers, which are either crosslinked or not crosslinked, are superior calcined clay slurry stabilizers both in their performance and because they obviate the need for additional dispersing agents. Acid-containing, alkali-soluble emulsion copolymers are particularly well suited to preparing stable suspensions and dispersions of calcined clay. The stable slurries of this invention may contain from 10 to 52%, and more preferably from 48 to 50%, by weight of calcined clay. In the pH range in which calcined clay slurries are made, typically from about pH 6 to about pH 8, there is a positive charge on the edges of the calcined clay particles. Acid-containing, anionic copolymers with high charge density which have been at least 50% neutralized can readily adhere to the surfaces of the clay particles and thereby act to inhibit agglomeration and dilatant settling. In addition, when the copolymers are alkali-soluble emulsions and are subjected to an aqueous solution of a controlled pH, the polymer chains uncoil. When uncoiled, polymer chains of sufficient length serve to thicken the slurry and enhance slurry stability. This can be accomplished by adjusting the pH to a value in the range from about pH 6 to about pH 8, with about pH 7 being preferred. The pH can be adjusted by the addition of caustic, such as sodium hydroxide, ammonium hydroxide, aluminum hydroxide or soda ash. It has been found that it is beneficial to have some hydrophobic character in the copolymer to enhance the compatibility of the copolymer with other organic compounds which may be present in the slurry (e.g. other stabilizers, dispersants, pigments, etc.). Hydrophobic character also enhances adsorption of the stabilizer on the hydrophobic surfaces of the calcined clay particles. Thus, while a polymer like polyacrylic acid may have a very high charge density, it lacks the degree of hydrophobic character necessary to make it an effective calcined clay slurry stabilizer. However, because of the large positive surface charge of calcined clay particles, it is desirable to have a significant amount of anionic character present in the copolymer. The copolymers used in this invention are alkali-soluble acrylic emulsion copolymers with high acid contents. The copolymers comprise from about 30% to about 60%, more preferably from about 33% to about 37%, by weight of the total polymer concentration of polymerized monomeric units of unsaturated noncarboxylic acids including alkyl esters of acrylic or methacrylic acids such as ethyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate, isobutyl methacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, hydroxyethyl acrylate, and hydroxypropyl acrylate. The more preferred unsaturated noncarboxylic add is ethyl acrylate. As used herein, in connection with the present invention, the term "noncarboxylic acid" refers to monomers which are copolymerizable with the comonomers used to form the copolymer and which have no free carboxylic acid groups. The comonomers comprise carboxylic acids. Preferred comonomers include monoethylenically unsaturated monocarboxylic acids containing from 3 to 6 carbon atoms per molecule and include acrylic acid, methacrylic add, vinyl acetic acid, crotonic acid and acryloxypropionic acid. The more preferred monoethylenically unsaturated monocarboxylic add is methacrylic acid. The concentration of these monomeric units in this invention is from about 70% to about 40%, and preferably from about 67% to about 63%, by weight of the total polymer concentration. The copolymer used in this invention can be polymerized using emulsion techniques well known to those skilled in the art. It has been found that copolymers with high charge density are effective stabilizers for calcined clay slurries with regard to settling and dilatancy. The charge density of the copolymers are quantitatively defined in terms of the acid equivalent weight of solids (AEWS). AEWS is the weight of polymer solids needed to neutralize one equivalent of base (i.e. 40 g. NaOH). Therefore, as the charge density increases, the AEWS value decreases. The AEWS values are determined by dividing the formula weight of the acid component by the relative amount of that component in the polymer. The copolymers used in this invention have AEWS values below 200 and more preferably below 150. Thus, for example, the AEWS value of a copolymer of 35% ethyl acrylate and 65% methacrylic acid, which is a suitable copolymer for use in slurries of the present invention, is calculated as follows: AEWS = Form. Wt. of MAA ÷ Rel. Amt. of MAA AEWS = 86 ÷ 0.65 = 132 Thus, it takes 132 g. of this copolymer to neutralize one equivalent of base in the manner described above. As a comparative example, a copolymer having a high AEWS value, therefore, a low charge density, is Acrysol (a trademark of the Rohm and Haas Company) ASE-60 crosslinked acrylic emulsion copolymer. Acrysol ASE-60 has an AEWS value of 215. Thus, it takes 215 g. of Acrysol ASE-60 copolymer to neutralize one equivalent of base in the manner described above. The copolymers used in this invention are alkali-soluble emulsion copolymers with high acid contents. It is to be understood that the term "emulsion copolymer", as used in connection with the present invention, refers to copolymers having a high molecular weight, for example, having a weight average molecular weight of at least 250,000 and preferably at least 500,000. Such high molecular weight copolymers are easily prepared as emulsions. Since non-emulsion copolymers of that molecular weight tend to be in the form of a gel, it is very difficult to economically prepare them as solution polymers. The copolymers used in this invention can be crosslinked, provided that they are not crosslinked to such an extent that the polymer network is insoluble. For example, the copolymers may be 0.03% by weight crosslinked copolymers. Either crosslinked or non-crosslinked copolymers will serve to stabilize suspensions and dispersions of calcined clay when present in amounts of from about 0.05% to about 1.0% by weight polymer solids on clay solids. More preferred are levels of copolymer from about 0.10% to about 0.25% by weight polymer solids and the most preferred is a copolymer level of about 0.20% by weight polymer solids. While it may be economically advantageous to make slurries at the highest clay solids possible, it is characteristic of calcined clay slurries to exhibit very steep rises in high shear viscosity at clay solids above 50%, making pumping and mixing operations unmanageable. For this reason, the calcined clay slurries of the illustrative Examples herein are made at 50% calcined clay solids by weight except where otherwise indicated. Stable calcined clay slurries of this invention can be made as either dispersed or non-dispersed slurries. Dispersed slurries may contain dispersing agents such as polyacrylic acid, sodium hexametaphosphate, sodium tripolyphosphate, tetrasodium pyrophosphate, sodium silicate, anionic polymers, anionic surfactants, nonionic surfactants, citric acid and salts thereof, ascorbic acid and salts thereof, alkali and alkanolamine soaps of fatty acids, other dispersing agents well known to those skilled in the art or combinations thereof. When used in dispersed calcined day slurries, high charge density alkali-soluble acrylic emulsion copolymers also show an increase in performance over polymers or copolymers with low charge density. Whether the slurries are dispersed with sodium hexametaphosphate or a 3,000 molecular weight homopolymer of acrylic acid, when they were stabilized with the higher charge density alkali-soluble acrylic emulsion copolymers, the stability of the slurries is enhanced. The pH of the slurries may, for example, be as in the following Examples, namely, in the range of from about pH 6 to about pH 8, with about pH 7 being preferred. The pH may be adjusted by the addition of sodium hydroxide. The slurries of this invention are useful as paper coatings, as fillers in paper manufacture, as paint additives, and as coatings for wire and cable. The following Examples are presented to illustrate preferred embodiments of the present invention. Example 1 (Comparative) Slurry 1: To 196.0 g. of water were added 50.0 g. of 0.75% (solids basis) carboxymethyl cellulose solution, 1.94 g. of 10% (solids basis) sodium hydroxide, and 0.6 g. of acrylic acid homopolymer in the sodium salt form having molecular weight of 3,000. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The viscosity and test results appear in Table I. Example 2 (Control) Slurry 2: To 196.0 g. of water were added 50.0 g. of 0.75% (solids basis) carboxymethyl cellulose solution. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. While mixing, enough of a 10% (by weight) sodium hydroxide solution was added to bring the pH of the slurry to the desired range. The slurry was then stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The viscosity and test results appear in Table I. Example 3 (Comparative) Slurry 3: 1.22 g. of 10% (by weight) sodium hydroxide was diluted to 20.g with water. 1.61 g. (product weight) of Acrysol ASE-60 crosslinked acrylic emulsion copolymer with an AEWS value of 215 was diluted to 230.0 g. with water. This latter mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The sodium hydroxide solution was then added and the slurry was mixed at low shear for 30 seconds. The viscosity and test results appear in Table I. Example 4 Slurry 4: 1.97 g. of 10% (by weight) sodium hydroxide was diluted to 20.g with water. 1.61 g. (solids basis) of an alkali-soluble acrylic emulsion copolymer of ethyl acrylate and methacrylic acid and an AEWS value of 132, was diluted to 230.0 g. with water. This latter mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The sodium hydroxide solution was then added and the slurry was mixed at low shear for 30 seconds. The viscosity and test results appear in Table I. Example 5 Slurry 5: 1.97 g. of 10% (by weight) sodium hydroxide was diluted to 20.g with water. 1.61 g. (product weight) of a 0.03% by weight crosslinked alkali-soluble acrylic emulsion copolymer of ethyl acrylate and methacrylic acid and an AEWS value of 132, was diluted to 230.0 g. with water. This latter mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The sodium hydroxide solution was then added and the slurry was mixed at low shear for 30 seconds. The viscosity and test results appear in Table I. Initial Viscosity Slurry Dosage (%) Low (cps) High (rpm) Flowability (%) Comments 1 0.26 486 455 96.4 Some soft 0.15 settled 2 0.15 590 243 not available Gelled 3 0.18 486 570 96.8 Some soft settled 4 0.20 354 n/a 98.1 Coating on walls 5 0.18 1060 505 98.1 Poured clean Table I shows a comparison of the slurries of the present invention with respect to the method of preparing a stable dispersion of calcined clay as taught in U.S.-A-4,017,324, wherein a dispersed calcined clay slurry was made using carboxymethyl cellulose and polyacrylic acid having a molecular weight of 3,000 and an AEWS value of 72, as the polymeric dispersant (slurry of Example 1). The slurry of Example 2 (control) represents a non-dispersed calcined day slurry which makes use of carboxymethyl cellulose as the only stabilizer, without the addition of any dispersing agent. The slurry of Example 3 illustrates the effect of a low charge density stabilizer alone in a non-dispersed calcined clay slurry. The slurry of Example 4 is a slurry of the invention resulting from the use of a high charge density stabilizer in a non-dispersed calcined clay slurry, and the slurry of Example 5 was a slurry of the invention resulting from the use of a crosslinked high charge density stabilizer in a non-dispersed calcined clay slurry. The results which appear in Table I show that the use of alkali-soluble acrylic emulsion copolymers with high charge density (low AEWS values) as stabilizers in calcined clay slurries give better performance with regard to dilatant settling than the stabilized systems previously known. Both the crosslinked and non-crosslinked stabilizers used to make the slurries resulted in comparable high shear viscosity values and better flowability values as compared to the dispersed system. As a control measure, the slurry made with carboxymethyl cellulose as a stabilizer failed to provide any stability to the slurry as indicated by the fact that the slurry gelled. Table II presents comparisons between dispersed calcined slurries made with different alkali-soluble acrylic emulsion copolymers. Each of the sets of data also compare the results of calcined clay slurries made with and without said copolymers. The calcined clay slurries appearing in Table II were made in the following way. The aqueous phase was prepared by mixing together the appropriate amount of a 1% (solids basis) copolymer solution to yield the desired dosage, sufficient base solution, NaOH (10% by weight), to equal 1.2 equivalents of base per equivalent of acid functionality contained in the added copolymer, an appropriate amount of dispersant, and enough water to yield 250 g. of solution. In the control experiments, where no stabilizer was added, the appropriate amount of dispersant was diluted to 250 g. with water and the pH was adjusted with a 10% (weight basis) sodium hydroxide solution after addition of the clay. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. When used in dispersed calcined clay slurries, high charge density, alkali-soluble, acrylic emulsion copolymers also show an increase in performance over the prior art as indicated by the data appearing in Table II. Whether the slurries were dispersed with sodium hexametaphosphate or a 3,000 molecular weight homopolymer of acrylic acid, when they were stabilized with the higher charge density alkali-soluble acrylic emulsion copolymers, the stability of the slurries was enhanced. Example 6 Slurry 8: To 196.0 g. water was added 37.5 g (1% solids basis) of a 0.03% by weight crosslinked, alkali-soluble, acrylic, emulsion copolymer of ethyl acrylate and methacrylic acid with an AEWS value of 132, 1.50 g. NaOH (weight basis) and 0.83 g. sodium hexametaphosphate. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. Example 7 (Comparative) Slurry 12: To 196.0 g. water was added 50.0 g (1% solids basis) of Acrysol ASE-60 crosslinked acrylic emulsion copolymer, an alkali-soluble acrylic emulsion copolymer with an AEWS value of 215, 1.10 g. NaOH (weight basis) and 0.83 g. sodium hexametaphosphate. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. Example 8 Slurry 17: To 196.0 g. water was added 50.0 g (1% solids basis) of an alkali-soluble acrylic emulsion copolymer of ethyl acrylate and methacrylic acid with an AEWS value of 132, 1.94 g. NaOH (weight basis) and 0.83 g. sodium hexametaphosphate. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. Example 9 Slurry 25: To 196.0 g. water was added 50.0 g (1% solids basis) crosslinked, alkali-soluble, acrylic emulsion copolymer of ethyl acrylate and methacrylic acid with an AEWS value of 132, 1.94 g. NaOH (weight basis) and 0.60 g. (solids basis) sodium salt of a homopolymer of acrylic acid having a molecular weight of 3,000. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. Example 10 (Comparative) Slurry 28: To 246.0 g. water was added 1.94 g. NaOH (weight basis) and 0.60 g. (solids basis) sodium salt of a homopolymer of acrylic acid having a molecular weight of 3,000. This mixture was stirred at low shear (low setting on a Waring Blender or 1,000 rpm on a Cowles mixer) and 250 g. of calcined kaolin clay was added slowly while mixing. After addition of the clay was complete, the slurry was stirred at high shear (high setting on a Waring Blender or 3,000 rpm on a Cowles mixer) for a sufficient time to achieve a homogeneous slurry. The results appear in Table II. The date appearing in Table III indicate the range over which an alkali-soluble acrylic emulsion copolymer with a low AEWS value is effective at stabilizing calcined clay slurries. Clay Solids, % Stabilizer Dosage, % Ambient Stability Hard Pack Flowable Syneresis Slurry 10 0.20 85.4 12.2 2.4 86.2 20 0.2 64.6 19.6 15.8 69.2 20 1.00 0 100 trace 98.3 30 0.2 20.2 61.8 18.0 74.6 40 0.2 6.2 92.5 1.3 98.2 50 0.2 1.4 98.6 0 98.1 52 0.2 1.6 88.7 9.7 80.1 50 0.3 1.5 98.5 0 97.6 50 0.4 0 100 0 96.3 Stable slurries were maintained over a wide range of day solids, from 10% to 52%. Also, the copolymers used in the slurries of this invention proved effective at stabilizing the slurries at levels of up to 1% polymer solids on a clay solids basis.

Claims: A stable calcined clay slurry, which comprises at least 10% by weight of calcined clay in an aqueous medium in the presence of 0.05% to 1.0% by weight, based on the total weight of solids, of anionic emulsion copolymer having an acid equivalent weight of solids value, determined by dividing the formula weight of the acid component by the relative amount of that component in the copolymer of less than 200 wherein the anionic emulsion copolymer comprises from 30% to 60% by weight of the total polymer concentration of polymerized monomeric units of unsaturated non carboxylic acids and from 40% to 70% by weight of the total polymer concentration of polymerized monomeric units of monoethylenically unsaturated monocarboxylic acid. A slurry as claimed in claim 1, wherein the anionic emulsion copolymer comprises from 30% to 60% by weight of polymerized monomeric units of alkyl ester of acrylic or methacrylic acid, and from 40% to 70% by weight of polymerized monomeric units of monoethylenically unsaturated monocarboxylic acid. A slurry as claimed in claim 2, wherein the anionic emulsion copolymer is an emulsion copolymer of ethyl acrylate and methacrylic acid, preferably an emulsion copolymer of 35% by weight ethyl acrylate and 65% by weight methacrylic acid. A slurry as claimed in claim 3, wherein the anionic emulsion copolymer is a 0.03% by weight crosslinked emulsion copolymer of 35% by weight ethyl acrylate and 65% by weight methacrylic acid. A slurry as claimed in any preceding claim, wherein the anionic emulsion copolymer has a weight average molecular weight of at least 250,000, preferably at least 500,000. A slurry as claimed in any preceding claim, wherein the concentration of the anionic emulsion copolymer is from about 0.10% to about 0.25%, preferably about 0.20%, by weight, based on the total weight of solids. A slurry as claimed in any preceding claim which has a pH of about 6 to about 8. A slurry as claimed in any preceding claim which comprises from 10% to 52% by weight of the calcined clay. A slurry as claimed in any preceding claim which is in the form of a suspension or dispersion. A slurry as claimed in claim 9 which is in the form of a dispersion and additionally comprises dispersing agent, preferably dispersing agent selected from polyacrylic acid, sodium hexametaphosphate, sodium tripolyphosphate, tetrasodium pyrophosphate, sodium silicate, anionic polymers, anionic surfactants, nonionic surfactants, citric acid and salts thereof, ascorbic acid and salts thereof, alkali and alkanolamine soaps of fatty acids, and combinations thereof. A process of making a stable calcined clay slurry as claimed in any preceding claim, which comprises:- (a) (i) when the slurry is to be formed as a suspension, dissolving in water the anionic emulsion copolymer; or (ii) when the slurry is to be formed as a dispersion, dissolving in water the anionic emulsion copolymer and, optionally, dispersing agent; (b) adding at least 10% by weight of calcined clay to the solution obtained in (a)(i) to provide a suspension, or to the solution obtained in (a)(ii) to provide a dispersion; and (c) adjusting the pH of the suspension or dispersion to a pH of about 6 to about 8. Use of a stable calcined clay slurry as claimed in any of claims 1 to 10, or as prepared by a process as claimed in claim 11, as a paper coating, a filler in paper manufacture, a paint additive, or as a coating for wire or cable.

Inventors: LEIN GEORGE MAX, MAHAR ROBERT CROUSE, LEIN, GEORGE MAX, MAHAR, ROBERT CROUSE
Applicants: ROHM & HAAS, ROHM AND HAAS COMPANY
Application year: 1991
Main classification: C09D17
IPC codes: C09K8, C09D17, C08F20, C08F220, B01J13, C04B33, C04B35, D21H17