Polysaccharides with alkaryl or aralkyl hydrophobes and latex compositions containing same

Abstract: Polysaccharides, including hydroxyethyl cellulose, having alkyl-aryl hydrophobic substitution, provide latex compositions, such as paints, with improved rheology and stability. Improved processes for producing such polysaccharides are also provided.

Description: This invention pertains to novel polysaccharides and their use in latex compositions and processes, and more particularly to cellulose ethers having alkyl-aryl hydrophobes, and improved processes for their production in which said cellulose ethers provide latex compositions with improved rheology and stability. Latex compositions typically have additives which modify the rheology or stability of the composition. Polysaccharides, and in particular cellulosics, have been described as additives to latex compositions for various purposes, including as protective colloids, thickeners, stabilizers or other rheology modifiers. For example, US-A-4,684,704 (Craig) describes latex compositions containing hydrophobically modified, hydroxyethyl cellulose as a protective colloid. US-A-4,243,803 (Landoll) and 4,352,916 (Landoll) describe the use of hydrophobically modified, hydroxyethyl cellulose as thickeners, emulsifiers and stabilizers for latex compositions. US-A-4,845,175 describes emulsion polymerization processes using hydrophobically modified hydroxyethyl cellulose, including alkyl-aryl-substituted materials. Polysaccharides having aryl substituents are known. For instance, US-A-1,451,331 (Dreyfus), 1,502,379 (Dreyfus), 1,589,607 (Lilienfeld), and 1,972,135 (Dreyfus) describe hydroxyethyl cellulose with aralkyl, e.g. benzyl, substitution. JP-A-82-28003 (Nakamura) describes benzyl substituted, quaternary nitrogen-containing cellulosics in cosmetics. US-A-4,663,159 (Brode, II et al.) describes water-soluble, cationic polysaccharides containing hydrophobes including aralkyl or alkaryl substituents, having various utilities. GB-A-1,228,850 describes a size for glass fibers containing a starch ether of a cyclic hydrocarbon or a substituted derivative thereof and a certain wax. SU-A-630,274 is directed to a laquer composition for finishing chrome leather which contains N-alkylarylaminooxypropylated cellulose acetate for improving the light resistance and the adhesion of the laquer film. According to EP-A-281951 certain alkyl-phenylcarbamate derivatives of polysaccharides are useful in the optical separation of racemic mixtures. This invention pertains to water-soluble cellulose ethers modified with a certain amount of alkyl-aryl hydrophobes (i.e., alkaryl or aralkyl groups having at least 10 carbon atoms) and to latex compositions using such modified cellulose ethers. The latex composition contains water, latex polymer and said water-soluble modified cellulose ether. Processes for producing these modified cellulose ethers are also provided. One process comprises reacting a cellulose ether with an alkyl-aryl hydrophobe containing compound wherein the ether substitution on the cellulose ether provides an increase in the amount of hydrophobe substitution reacted onto the cellulose ether. Another process comprises reacting a polysaccharide with an alkyl-aryl hydrophobe-containing glycidyl ether compound. The present modified cellulose ethers have one or more alkyl-aryl substituents with at least 10, preferably from 12 to 24, and most preferably from 15 to 18, carbon atoms in the alkyl-aryl group, i.e. hydrophobe. The aryl portion of the hydrophobe may have one or more aryl rings, which may be fused, carbocyclic or heterocyclic, unsubstituted or substituted with other functional groups, such as halogen, nitro, hydroxyl, amino or other substituents. The alkyl portion of the hydrophobe may be straight or branched chain, cyclic or acyclic, saturated or partially unsaturated, unsubstituted or substituted with other functional groups, such as halogen, hydroxyl or other substituents. Alkyl-aryl hydrophobes include both aralkyl or alkaryl groups. Typical hydrophobes include, but are not limited to, one or more of the following: alkaryl such as t-butylphenyl, nonylphenyl or dodecylphenyl; and aralkyl such as phenylhexyl or naphthyldodecyl. Preferred hydrophobes are nonylphenyl and dodecylphenyl. The degree of hydrophobe substitution, i.e. DS, defined as the average moles of hydrophobe substituent per mole of cellulose ether repeat unit, may vary depending upon the presence of other substituents and type of hydrophobe, In any event, the DS of the hydrophobe is from 0.001 to 0.1, and most preferably from 0.005 to 0.03. The cellulose ethers with alkyl-aryl hydrophobes include polymers of repeating units represented by the structural formula: In Formula I, for each repeating unit individually: Q is -O-, wherein R₄ is or a mixture of hydrogen and R sacch is the residue of a cellulose repeat unit and may include additional reactive groups; x is from 50 to 20,000; each y₁, y₂ and y₃ is 0 or 1; each Z₁, Z₂ and Z₃ is a divalent connecting segment; and each R₁, R₂ and R₃ is individually a hydrogen, an unsubstituted or a nitrogen-, oxygen-, sulfur- or carboxyl-containing hydrocarbyl group or R h , wherein R h is an alkyl-aryl hydrophobe, provided that (1) when R₁, R₂ or R₃ is hydrogen then y₁, y₂ or y₃, respectively is 0 and (2) one or more repeating units have one or more R₁, R₂ or R₃ which is R h . In Formula I, Q is oxygen providing cellulose repeat units. The number of repeat units, defined by x, is preferably from 50 to 20,000 and most preferably from 250 to 4,000, providing a molecular weight of from several thousand up to several million. The molecular weight of the cellulose ether may be varied using well established procedures, such as controlled degradation. In Formula I, the ether substituents, i.e. are usually hydrogen with some alkyl-aryl hydrophobes, and preferably hydroxyethyl, present. Since only one or more repeating units must have one or more R h , not every cellulose ether repeat unit must have an alkyl-aryl hydrophobe. Generally, only a minor portion of repeat units will have one or more hydrophobes. Typical ether substituents include, but are not limited to, one or more of the following: hydrogen, i.e. -H; unsubstituted hydrocarbyl such as -CH₃, -CH₂CH₃, -CH₂C₆H₅, or -C₁₆H₃₃; nitrogen-, oxygen-, sulfur- or carboxyl-containing hydrocarbyl such as -CH₂CH₂OH; -CH₂COOH; -CH₂COO⁻Na⁺ or alkyl-aryl hydrophobes with or without connecting segments, including the alkyl-aryl hydrophobes described previously, such as Preferably the ether substituents also include hydroxyethyl, i.e. -CH₂CH₂OH, in an amount sufficient to provide water solubility. In Formula I, the divalent connecting segment, represented by Z₁, Z₂ and Z₃, designates the portion of the ether substituent which is provided between the cellulose ether oxygen and the main portion of the substitutent, such as an alkyl-aryl group. When R₁, R₂ or R₃ is hydrogen, i.e. when the group represented is an unsubstituted hydroxyl, there is no connecting segment and y₁, y₂ or y₃ is correspondingly 0. When R₁, R₂ or R₃ is not hydrogen, then a connecting segment may or may not be provided. Generally, the connecting segment represents the residual portion of the compound used to provide an alkyl-aryl substitutent on the cellulose ether, which portion is not the alkyl-aryl group per se . Typical connecting segments, when present, include, but are not limited to: unsubstituted or hydroxy-substituted alkyl or alkoxy groups such as methylene, i.e. -CH₂-, ethoxy, i.e. -CH₂CH₂O-, or glycidyl ethers, i.e. Preferably, the connecting segment is absent or present as -CH₂- or most preferably as The cellulose ether may contain additional substitution, i.e. other than the hydrophobes, such as may be required to provide the requisite water solubility or other properties. The other substituents may be ionic or nonionic providing nonionic, cationic, anionic or amphoteric polysaccharide. Typical additional substituents include, but are not limited to, one or more of the ether substituents described previously. The amount of additional substitution, i.e. molar substitution defined as the average moles of such substituent per mole of cellulose ether repeat unit, designated MS, is not critical but may be any amount desired. Preferably, the cellulose ether will have a hydroxyethyl MS sufficient to provide water solubility, if needed, and/or improved enzyme resistance if desired. Hydroxyethyl MS may generally be from 1.5 to 6, and preferably from 3 to 5. The hydrophobe-substituted cellulose ethers can be produced from readily available cellulose ether starting materials which may be derived from conventional materials, such as chemical cotton, cotton linters, wood pulp, alkali cellulose, as well as ether derivatives of these materials. Cellulose ethers which may be used include, but are not limited to, one or more of the following: hydroxyethyl cellulose; hydroxypropyl cellulose; methyl cellulose; carboxymethyl cellulose; carboxyethyl cellulose; hydroxypropyl ethyl cellulose; hydroxyethyl carboxymethyl cellulose; and the like. A particularly preferred cellulose ether is hydroxyethyl cellulose. Any reaction condition sufficient to modify the cellulose ether with the hydrophobes may be used, including well established etherification procedures, such as described in US-A-4,663,159 (Brode, II, et al.) or 4,228,277 (Landoll). This reaction may be conducted using any compound having the hydrophobe and a functional group which reacts with the cellulose ether. Typical functional groups include, but are not limited to, one or more of the following: halides, such as chlorides or bromides; oxiranes, such as epoxides including glycidol and its esters; acids, including esters, acid halides or salts thereof, such as carboxylic acids or sulfates; (thio)isocyanates; and halohydrins. Alkyl-aryl halides may be used but may not be desirable due to problems with corrosivity and having to remove halides from the product. Preferably a glycidyl ether, such as nonyl- or dodecylphenyl glycidyl ether, is used. The hydrophobe substitution reaction may be conducted at any desired temperature, typically between 20°C to 125°C and preferably from 55°C to 95°C, for a time sufficient to provide the desired amount of substituents, typically from 0.5 hour to 12 hours or more and preferably from 1 to 6 hours. The reaction may be conducted with diluent, solvent or catalyst as desired and is typically done in an inert medium in the presence of a caustic catalyst, such as an alkali metal hydroxide or the like material. In a preferred embodiment, the hydrophobe substitution is conducted by reacting a compound, having an alkyl-aryl group with a cellulose ether containing another substituent, such as hydroxyethyl, in an amount which increases the efficiency of hydrophobe substitution. The MS of other ether substitution, i.e. MS E , may vary depending upon the types of cellulose ether, hydrophobe and other ether substituents present and is generally at least that amount which provides increased hydrophobe substitution as compared to an MS E of 0. In embodiments when the other ether substituent is hydroxyethyl, MS E may range from greater than 0, preferably from 1.5 to 6 and most preferably from 3.5 to 5 average moles of other ether substituent per mole of cellulose ether repeat unit. In another preferred embodiment, the hydrophobe substitution is conducted using an alkyl-aryl compound having a functional group which is a glycidyl ether. Such compounds may be represented by the structual formula: wherein R h is an alkyl-aryl hydrophobe as defined previously, in Formula I. Substitutions using such compounds have been found to provide higher reaction efficiencies when compared to other functional groups, including the closely related, corresponding epoxides, such as represented by the structural formula: wherein R h is as previously defined. While not bound to any particular theory, the increased reaction efficiencies provided by alkyl-aryl glycidyl ethers may be due to higher reactivity of glycidyl ether groups to nucleophilic attack by the cellulose ether. In a typical procedure the hydrophobe substitution reaction is carried out in a slurry of the desired cellulose ether in an appropriate aqueous diluent system. Suitable diluents include, but are not limited to, isopropyl alcohol, t-butyl alcohol, sec-butyl alcohol, propyl alcohol, ethanol, methanol, methylethylketone, water, tetrahydrofuran, dioxane, 2-butoxyethanol, 2-ethoxyethanol, acetone, and mixtures of these materials. Suitable weight ratios of diluent to polysaccharide are in the range of 4:1 to 25:1. Because the reaction is generally carried out heterogeneously, it is important that the diluent system normally not be a solvent for either the starting cellulose ether or the hydrophobe-modified product. The cellulose ether may be causticized with a suitable caustic catalyst such as sodium hydroxide, potassium hydroxide or lithium hydroxide, with sodium hydroxide being preferred. The molar ratio of caustic to cellulose ether may suitably vary between 0.4 to 2.0. Many polysaccharides that are in contact with any base may be readily degraded by oxygen. It is accordingly necessary to exclude oxygen from the reaction vessel during the time in which caustic is present. It is suitable to carry out the reaction under an inert gas such as nitrogen. After being causticized with a suitable amount of caustic catalyst, the hydrophobic reactant may be added, and the reaction is conducted at a suitable temperature for a time sufficient to provide the desired amount of substitution. Alternately, the cellulose ether may be first reacted with one or more appropriate electrophiles to render it water-soluble followed by a sequential reaction with the hydrophobic reactant, or it may be simultaneously reacted with one or more electrophiles and the hydrophobic reactant. Suitable electrophiles include ethylene oxide, propylene oxide, chloroacetic acid and its salts, 1,3-propane sultone, methyl chloride, ethyl chloride, glycidol, 3-chloro-1,2-propanediol, and 2-chloroethanol. Latex compositions can be provided having as essential components: water; latex polymer; and the modified cellulose ether. The kind and amount of latex polymer is not critical, and may be provided based on well established procedures. Typical latex polymers include, but are not limited to, various types such as the following: acrylics; alkyds; celluloses; coumarone-indenes; epoxys; esters; hydrocarbons; maleics; melamines; natural resins; olefin resins; phenolics; polyamides; polyesters; rosins; silicones; styrenes; terpenes; ureas; urethanes; vinyls; and the like. Illustrative latex polymers include, but are not limited to, one or more homo- or copolymers containing one or more of the following monomers: (meth)acrylates; vinyl acetate; styrene; ethylene; vinyl chloride; butadiene; vinylidene chloride; vinyl versatate; vinyl propionate; t-butyl acrylate; acrylonitrile; neoprene; maleates; fumarates; and the like, including plasticized or other derivatives thereof. The amount of modified cellulose ether which may be used in the latex composition is not narrowly critical. In the broadest sense, the amount of modified cellulose ether is that which is an effective amount in providing improved rheology or stability to the latex composition. Typically, the amount of modified cellulose ether is at least 0.05, preferably from 0.15 to 3, and most preferably from 0.25 to 1.5 weight percent of the latex composition. The amount of latex polymer used in the latex composition is not critical, but may be any amount following well established procedures using latex polymers. Typically, the amount of dry latex polymer is at least 1, preferably from 2 to 50, and most preferably from 3 to 40 weight percent of the total latex composition. The latex composition may optionally contain other components such as those generally used in latex compositions. Typical components include one or more of the following: solvents such as aliphatic or aromatic hydrocarbons, alcohols, esters, ketones, glycols, glycol ethers, nitroparaffins or the like; pigments; fillers, dryers; flatting agents; plasticizers; stabilizers; dispersants; surfactants; viscosifiers including polymeric associative thickeners, polysaccharide-based thickeners and so on; suspension agents; flow control agents; defoamers; anti-skinning agents; preservatives; extenders; filming aids; crosslinkers; surface improvers; corrosion inhibitors; and other ingredients useful in latex compositions. Processes for producing latex compositions having improved rheology and stability can be provided by combining the latex polymer and modified cellulose ether with water following established procedures. Although not bound by any particular theory it is believed that the modified cellulose ethers control the rheology of the latex composition by two mechanisms. As with other cellulosics, the aqueous phase of the composition is thickened by the presence of a large hydrodynamic volume resulting from the relatively high molecular weight and water of hydration surrounding the modified cellulose ether. The alkyl-aryl substitution also thickens the latex composition by an associative mechanism wherein the hydrophobes interact with each other and hydrophobic portions of the latex polymer or other ingredients present resulting in improved properties such as high viscosity at low shear, improved spatter resistance and improved flow and leveling, while avoiding problems with syneresis, color acceptance, color development and viscosity stability. Latex compositions using the modified cellulose ethers are provided whereby the modified cellulose ether may be used as a protective colloid, thickener, stabilizer or other rheology modifier, such as for emulsion polymerization. The modified cellulose ethers may also be used in a variety of applications other than in latex compositions and processes. Additional applications include, but are not limited to: cosmetics, such as shampoos; biomedicine such as in oral care including toothpaste or in pharmaceuticals including timed- or controlled-release formulations; detergents such as in laundry or surface cleaners; various other timed-release applications including pesticides; and other areas in which a protective colloid, stabilizer, thickener or rheology modifier is desired. This invention is further illustrated in the following examples, which are merely representative of various embodiments within the scope of the claims. Unless stated otherwise, all percentages correspond to weight percent. EXAMPLES The designations and abbreviations used in the examples are defined as follows: Designation Description C₁₆ Epoxy 1,2-epoxyhexadecane (CAS#7320-37-8). EO Ethylene oxide. NPGE Nonylphenyl glycidyl ether, distributed under the trademark of HELOXY® WC-64 by Wilmington Chemical Company. Wood pulp Commercially flocked RAYONIER® X-F, ETHANIER® F or ETHANIER® F-HV wood pulp, as specified. SLS Sodium lauryl (dodecyl) sulfate. HEC-1 Hydroxyethylcellulose, prepared from wood pulp, having an EO MS of about 3.5. HEC-2 Hydroxyethylcellulose having a 5% solution viscosity (Brookfield, spindle #1, 30 rpm) of about 125 mPa·s (cP), available from Union Carbide Corporation under the tradename of CELLOSIZE® QP-09L. HEC-3 Hydroxyethylcellulose, having a 2% solution viscosity (Brookfield, spindle #2, 30 rpm) of about 400 mPa·s (cP), available from Union Carbide Corporation under trademark of CELLOSIZE® WP-300. HEC-4 Hydroxyethylcellulose, having a 1% solution viscosity (Brookfield, spindle #3, 30 rpm) of about 400 mPa·s (cP), available from Union Carbide Corporation under trademark of CELLOSIZE® ER-4400. GTMAC A 70% aqueous solution of glycidyl trimethylammonium chloride, available from Degussa under the trademark of QUAB-151. SCA Sodium chloroacetate. The following test procedures describe the characterization of the cellulose ethers with alkyl-aryl hydrophobes, and define the performance tests used in their evaluation. EO MS : The molar substitution of EO in the cellulose ethers is determined from the mass gain of the product, corrected for ash and volatiles. EO MS is given by: where Mf is the total mass of product, corrected for ash and volatiles. NPGE DS : Approximately 0.2 g of the cellulose ether (weighed to the nearest 0.1 mg, recorded as m , and corrected for volatiles and ash) is dissolved in water containing 0.5 g of 30% aqueous SLS and diluted to 50.00 ml. The ultraviolet spectrum from 300 to 240 nm is recorded, and the absorbance at 278 nm is recorded as A (corrected for the baseline, e = 1530 M⁻¹cm⁻¹). The EO MS is given by y , so that the NPGE DS is given by: 1% Viscosity : Viscosity, in mPa·s (centipoise), of an aqueous solution of the cellulose ether at 1% measured using a Brookfield viscometer, model LVT, spindle #2, at 30 rpm and 25°C. Stormer viscosity : ASTM Method D 562. ICI viscosity : Viscosity, in 10⁻¹ Pa·s (poise), measured on the final latex paint formulation using an ICI Cone and Plate Viscometer, Model VR-4000. Brookfield viscosity : ASTM Method D 2196-81. The data in Table 2 are divided by 1000, so that, for example, 25.3 is equivalent to 25,300 mPa·s (cP). Sag resistance : ASTM Method D 4400-84. Leveling : ASTM Method D 4062-81. Contrast ratio : A 0.1 mm (4 mil) wet film of the latex paint is cast onto an opacity chart (Leneta, 3B Opacity chart) and allowed to dry for 24 hours. The percent reflectance of the paint over the black portion (Rb) and white portion (Rw) of the chart is recorded. The contrast ratio is reported to three significant figures, and is given by: Contrast ratio = Rb Rw Spatter resistance : ASTM Method D 4707-87. Examples 1-35: Cellulose ether Substitution Various cellulose ethers with alkyl-aryl hydrophobes are prepared using one of several procedures. i.e. Synthesis Methods A, B, C, D or E. The specific preparations are set forth in Table I. Synthesis Method A A 1.4 l (three pint) glass pressure reactor is charged with 25.0 g of wood pulp in the designated diluent system. The mixture is stirred for one hour while purging the head space of the reactor with nitrogen to remove any entrained oxygen. After 30 minutes, the reactor is warmed to 32°C. While at 32°C, 22% aqueous sodium hydroxide is added under nitrogen. The slurry is then stirred at 35°C under nitrogen for one hour. Freshly distilled EO is added to the reactor, which is then sealed and heated to 75°C. Timing of the ethoxylation is begun at the onset of 75°C. Thirty minutes after reaching 75°C, a solution of 30% hydrogen peroxide in 5 ml of water is added. The reaction is continued at 75°C for 2.5 hours. NPGE is added to the reactor and the injection line is rinsed with 10 ml of acetone. The reaction is continued at 75°C for six more hours. The total reaction time at 75°C is nine hours. The reactor is cooled to room temperature and 9.5 g of glacial acetic acid is added. The mixture is stirred for 15 minutes, and the cellulose ether is recovered by vacuum filtration. The cellulose ether is washed in a Waring® blender: five times with 500 ml of 5:1 (by volume) acetone/water, and twice with 500 ml of acetone. The polymer is dried overnight in vacuo at 50°C. Synthesis Method B A 1.4 l (three pint) glass pressure reactor is charged with 25.0 g of wood pulp, 353.3 g of acetone, 37.0 g of water, and 59.7 g of ethanol. The mixture is stirred for one hour while purging the head space of the reactor with nitrogen to remove any entrained oxygen. After 30 minutes, the reactor is warmed to 32°C. While at 32°C, 22% aqueous sodium hydroxide is added under nitrogen. The slurry is then stirred at 35°C under nitrogen for one hour. NPGE and freshly distilled EO in 16 ml of acetone are added to the slurry. The reactor is sealed, and the mixture is heated at 75°C for twelve hours. The reactor is then cooled, and 4.00 g of glacial acetic acid is added. After stirring the slurry for 15 minutes, the product is isolated and washed as described in Method A. Synthesis Method C A 1.4 l (three pint) glass pressure reactor is charged with wood pulp, acetone, ethanol, and water as described in Method A. The mixture is stirred for one hour while purging the head space of the reactor with nitrogen, and warmed to 32°C, as described in Method A. While at 32°C, 22% aqueous sodium hydroxide is added under nitrogen. The slurry is then stirred at 35°C under nitrogen for one hour. Freshly distilled EO is added to the reactor, which is then sealed and heated to 75°C. After one hour, the reactor is cooled to 25°C. 11.2 g of glacial acetic acid is added, and the slurry stirred for 5 minutes. Then, NPGE and the second charge of freshly distilled EO are added to the slurry. The reactor is sealed, and the mixture is heated at 75°C for six hours. The slurry is cooled, and 5.6 g of 50% aqueous sodium hydroxide is added to the slurry. After stirring ten minutes, a solution of hydrogen peroxide in 10 ml of water is added, and the mixture is heated at 55°C for one hour. The mixture is cooled, 12.0 g of glacial acetic acid is added, and the slurry is stirred for 15 minutes. The product is then isolated and washed as described in Method A. Synthesis Method D A 1.4 l (three pint) glass pressure reactor is charged with 25.0 g of wood pulp and the designated diluent system. The mixture is stirred for one hour while purging the head space of the reactor with nitrogen to remove any entrained oxygen. After 30 minutes, the reactor is warmed to 32°C. While at 32°C, 22% aqueous sodium hydroxide is added under nitrogen. The slurry is then stirred at 35°C under nitrogen for one hour. Freshly distilled ethylene oxide is added to the reactor, which is then sealed and heated to 85°C. Timing of the ethoxylation is begun at the onset of 85°C. Thirty minutes after reaching 85°C, a solution of 30% hydrogen peroxide in 5 ml of water is added. The reaction is continued at 85°C for 1.5 hours. NPGE is added to the reactor, and the injection line is rinsed with 10 ml of acetone. The reaction is continued at 85°C for three more hours. The total reaction time at 85°C is five hours. The reactor is cooled to room temperature and 9.5 g of glacial acetic acid is added. The mixture is stirred for 15 minutes, and the cellulose ether is recovered by vacuum filtration. The cellulose ether is washed in a Waring® blender: five times with 500 ml of 5:1 (by volume) acetone/water, and twice with 500 ml of acetone. The polymer is dried overnight in vacuo at 50°C. Synthesis Method E A 250 ml. three-necked round bottomed flask is fitted with a stirring paddle and motor, a rubber serum cap, a nitrogen inlet, a pressure-equalizing addition funnel, and a Friedrich condenser with a mineral oil bubbler. The flask is charged with the designated polysaccharide and diluent. The slurry is stirred for one hour while purging the head space of the reactor with nitrogen to remove any entrained oxygen. Aqueous sodium hydroxide solution (50%, by weight) is added to the slurry under nitrogen, and the slurry is stirred under nitrogen for one hour. Heat is applied to the slurry up to 55°C and NPGE, and other reactant as noted in Table 1, are added to the slurry under nitrogen. The mixture is maintained at 55°C for the specified time, cooled to ambient temperature, and neutralized with 4.0 g of glacial acetic acid. After stirring for 15 minutes, the product was collected by vacuum filtration and washed and dried as described previously. Examples 35-36: Cellulose Ether Enhancement of Hydrophobe Substitution A 250 ml, three-necked round bottomed flask is fitted with a stirring paddle and motor, a rubber serum cap, a nitrogen inlet, a pressure-equalizing addition funnel, and a Friedrich condenser with a mineral oil bubbler. The flask is charged with HEC, as designated in Table 2, 68.5 g of acetone, 12.0 g of ethanol, and 7.0 g of water. While stirring the slurry, the headspace of the flask is purged with nitrogen for one hour to remove any entrained oxygen. A 50% aqueous sodium hydroxide solution is added to the slurry by syringe, and the slurry is stirred for 90 minutes. A solution of NPGE in 7.4 g of acetone is then added and the mixture is refluxed at ambient pressure for 24 hours. The slurry is cooled to room temperatures and a solution of 2.0 g of glacial acetic acid in 15 ml of acetone is added to the slurry with stirring. After 15 minutes, the cellulose ether is recovered by vacuum filtration and washed three times in a Waring® blender with 300 ml of acetone. The polymer is dried in vacuo at 50°C overnight. The hydrophobe content, i.e., NPGE DS, is determined using the previously described procedure. It is evident from these experiments that under identical reaction conditions, higher hydrophobe alkylation efficiencies are observed with cellulose ethers having higher EO MS values. Example Cellulose Ether Caustic NPGE (g) Yield (g) NPGE DS Substitution Efficiency Mass EO MS (g) Mole Ratio 35 12.4 3.5 1.58 0.50 2.63 15.5 0.059 24% 36 12.3 2.3 1.85 0.49 3.10 13.1 0.025 10% Examples 37 and B : Glycidyl Ethers Enhancement of Reaction Efficiency A 1.4 l (three pint), glass pressure reactor is charged with 25.0 g of wood pulp, 353.3 g of acetone, 60.8 g of ethanol and 36.0 g of water. The mixture is stirred for one hour while purging the head space of the reactor with nitrogen to remove any entrained oxygen. After 30 minutes, the reactor is warmed to 32°C. While at 32°C, aqueous sodium hydroxide is added to the slurry under nitrogen. After stirring the slurry at 35°C under nitrogen for one hour, the hydrophobic reactant specified in Table 3 and freshly distilled ethylene oxide in 16 ml of acetone are added. The reactor is sealed, and the mixture is heated at 75°C for six hours. The reactor is cooled to room temperature, and 18.75 g of glacial acetic acid is added. After stirring for 15 minutes, the polymer is isolated and washed as described in Synthesis Method A. Example Caustic EO Hydrophobe Substitution (g) Ratio (g) Ratio Type (g) DS Efficiency 37 43.2 1.54 40.0 3.2 NPGE 10 0.007 3.0% B 47.5 1.54 47.5 3.8 C₁₆ Epoxy 15 0.004 1.1% The results in Table 3 show that despite using twice the molar charge of hydrophobic compound, the control Example B provided significantly less hydrophobic substitution as compared to the glycidyl ether compound in Example 37. Examples 38-39: Latex Formulations and Evaluations Latex Paint Screening Formulation Pigment Grind: Component kg (Pounds) Liter (Gallons) Water 58.6 (129.3) 59.0 (15.52) PROXEL (R) GXL (preservative) 0.45 (1.0) 0.49 (0.13) TAMOL (R) 731 (dispersant) 7.7 (17.0) 7.03 (1.85) PAG 188 (defoamer) 0.82 (1.8) 0.95 (0.25) TERGITOL (R) NP-10 (surfactant) 0.45 (1.0) 0.42 (0.11) TiPure (R) R-931 (TiO₂ pigment) 68.0 (150.0) 18.8 (4.95) Satintone (R) W (clay extender) 56.6 (125.0) 22.1 (5.81) Camel Carb (R) (CaCO₃) 68.0 (150.0) 24.5 (6.45) Water 9.1 (20.0) 9.1 (2.40) Let Down: Component kg (Pounds) Liter (Gallons) UCAR (R) Latex 376 112.6(248.5) 104.3 (27.46) Texanol (R) (filming aid) 3.6 (7.9) 3.8 (1.00) 28% aqueous ammonia 0.95 (2.1) 0.95 (0.25) PAG 188 (defoamer) 0.82 (1.8) 0.95 (0.25) Designated Polysaccharide 1.8-2.7(4-6) 1.3-2.0 (0.35-0.52) Propylene glycol 6.3 (14.0) 6.15 (1.62) Water 118.6-119.2 (261.8-263.2) 119.4-120.0 (31.43-31.60) 514.9-515.2 (1,136.6-1,137.2) 380.00 (100.00)

Claims: Claims for the following Contracting States : AT, BE, DK, FR, GR, IT, LU, NL, SE, CH, LI, GB, DE A water-soluble cellulose ether modified by substitution with an alkaryl or aralkyl group having at least 10 carbon atoms in an amount of on the average 0.001 to 0.1 moles of said alkaryl or aralkyl group per mole of cellulose ether repeat unit. The cellulose ether of claim 1 wherein the alkaryl or aralkyl substituent has from 12 to 24 carbon atoms. The cellulose ether of claim 1 wherein the alkaryl or aralkyl substituent is selected from t-butylphenyl, nonylphenyl, dodecylphenyl, phenylhexyl and naphthyl-dodecyl. The celllulose ether of claim 3 wherein the alkaryl substituent is nonylphenyl or dodecylphenyl. The cellulose ether of claim 1 which comprises 50 to 20000 cellulose ether repeat units. The cellulose ether of claim 1 wherein the average amount of alkaryl or aralkyl group is 0.005 to 0.03 moles per mole of cellulose ether repeat unit. The cellulose ether of claim 1 which is modified hydroxyethyl cellulose. The cellulose ether of claim 7 having a molar substitution of on the average 1.5 to 6 moles of ethyleneoxy groups per mole of cellulose ether repeat unit. The cellulose ether of claim 1 wherein the ether substituent is selected from -CH₃, -CH₂CH₃, -CH₂C₆H₅, -C₁₆H₃₃, -CH₂CH₂OH and -CH₂COOH. A process for producing the modified cellulose ether of claim 1 which comprises reacting a cellulose ether having a molar substitution of on the average 3-5 moles of ether groups per mole of cellulose ether repeat unit with a compound containing an alkaryl or aralkyl group having at least 10 carbon atoms in an amount sufficient to provide a correspondingly modified cellulose ether having on the average 0.001 to 0.1 moles of said alkaryl or aralkyl group per mole of cellulose ether repeat unit. The process of claim 10 wherein the cellulose ether is hydroxyethyl cellulose and the compound containing an alkaryl or aralkyl group is an alkaryl glycidyl ether. A latex paint composition containing water, latex polymer and the modified water-soluble cellulose ether of any one of claims 1 to 9. The latex paint composition of claim 12 which contains 0.15 to 3 weight percent of said modified cellulose ether. Claims for the following Contracting State : ES A process for producing a water-soluble cellulose ether modified by substitution with an alkaryl or aralkyl group having at least 10 carbon atoms in an amount of on the average 0.001 to 0.1 moles of said alkaryl or aralkyl group per mole of cellulose ether repeat unit which process comprises reacting the starting cellulose ether with a compound containing said alkaryl or aralkyl group and a group which reacts with the cellulose ether in an amount sufficient to afford the above average degree of substitution of the cellulose ether. The process of claim 1 wherein the alkaryl or aralkyl substituent has from 12 to 24 carbon atoms. The process of claim 1 wherein the alkaryl or aralkyl substituent is selected from t-butylphenyl, nonylphenyl, dodecylphenyl, phenylhexyl and naphthyl-dodecyl. The process of claim 3 wherein the alkaryl substituent is nonylphenyl or dodecylphenyl. The process of claim 1 wherein the cellulose ether comprises 50 to 20 000 cellulose ether repeat units. The process of claim 1 wherein the average amount of alkaryl or aralkyl group is 0.005 to 0.03 moles per mole of cellulose ether repeat unit. The process of claim 1 wherein hydroxyethyl cellulose is modified. The process of claim 7 wherein a cellulose ether having a molar substitution of on the average 1.5 to 6 moles of ethyleneoxy groups per mole of cellulose ether repeat unit is employed. The process of claim 1 wherein the ether substituent is selected from -CH₃, -CH₂CH₃, -CH₂C₆H₅, -C₁₆H₃₃, -CH₂CH₂OH and -CH₂COOH. The process of claim 1 wherein a cellulose ether having a molar substitution of on the average 3 to 5 moles of ether groups per mole of cellulose ether repeat unit is used as starting material. The process of claim 10 wherein the cellulose ether is hydroxyethyl cellulose and the compound containing said alkaryl or aralkyl group is an alkaryl glycidyl ether. A latex paint composition containing water, latex polymer and the modified water-soluble cellulose ether prepared according to the process of any one of claims 1 to 11. The latex paint composition of claim 12 which contains 0.15 to 3 weight percent of said modified cellulose ether.

Inventors: BRODE GEORGE LEWIS II, HOY RICHARD CHARLES, PARTAIN EMMETT MALONE III, BRODE, GEORGE LEWIS, II, HOY, RICHARD CHARLES, PARTAIN, EMMETT MALONE, III
Applicants: UNION CARBIDE CHEM PLASTIC, UNION CARBIDE CHEMICALS AND PLASTICS COMPANY, INC.
Application year: 1990
Main classification: C08B37
IPC codes: C08B11, C08B15, C09D7, C08B13, C08L1, C08B37