Aqueous polymer dispersions

Abstract: A water miscible, stable, fluid product comprises parti­ cles above 20 microns in size of a high molecular weight polymer gel interconnected by a continuous phase that is an aqueous solution of an equilibrating agent that holds the water contect of the particles in equilibrium with the water content of the aqueous phase and that prevents substantial agglomeration of the particles in the fluid product. Preferred equilibrating agents are sodium polyacrylate and poly-diallyl dimethyl ammonium chloride.

Description: High molecular weight water soluble polymers are useful in various applications, such as flocculation, for example waste water, or in paper making, thickening and coating applications. In most applications the polymer is used as a dilute aqueous solution at a concentration in the range 0.05 to 2.0% by weight. It is impractical to produce and transport such dilute solutions. Concentrated solutions are viscous and difficult to handle. Aqueous gels are also difficult to handle and to dilute and have low solids content compared to dry solids. Dry solids formed from aqueous gels require high energy expenditure in comminution and drying processes or use of undesirable inflammable solvents and may cause dusting problems. Various methods for producing liquid products having a high concentration of polymers have been proposed. In U.S. 3,734,873 a water-in-oil emulsion containing aqueous polymer particles in a non-aqueous liquid including oil-in-water emulsifier is described. In GB 1,397,933 there is described a method of dispersing solid polymer into oil to give a fluid dispersion. In US 3,985,651 dry polymer is dispersed in a polyhydric alcohol in which it is not soluble. In US 4,118,355, a dry polymer is dispersed in one or a blend of water-miscible solvents (e.g., methanol and a glycol ether), in which it is insoluble but it dissolves in the presence of water. Although these liquid products avoid many of the disadvantages of dilute solutions, gels and dry solids they incur the disadvantage that they include materials, for instance organic solvent and/or surfactant, that is generally unwanted at the place of use and may be positively undesirable. For instance the incorporation of oil or other organic solvents is undesirable when the products are being used in the solvent extraction of mineral values or in drilling muds for the oil industry and incorporation of surfactants is undesirable when the products are being used for the treatment of aqueous systems since the resultant water will contain surfactant and this may cause foaming or toxicity problems, especially when the water is eventually discharged into the environment. Also the use of organic solvents is expensive and can cause safety hazards during manufacture. These liquid products often contain a stabiliser for stabilising the dispersion of polymer particles in the organic solvent. Stabilisers for polymer dispersions generally act by forming a protective film of water insoluble material around the polymer particles. Suitable materials are described in British Patent Specification No. 1,482,515. The continuous phase of the liquid products has to be non-aqueous since the polymer, being water swellable or water soluble, would otherwise dissolve partially or completely in the continuous phase and would form either a very viscous solution or an agglomerated mass. In US Patent Specification 4,380,600 a dispersion of certain water soluble polymers in aqueous media is made by polymerisation in the presence of certain, different, water soluble polymers, the amounts of water, monomer and polymer being within defined limits. The polymer is said to be present as microscopic particles and so presumably the particle size is at the most, only a few µm. It is essential to the process that the polymer made during the process is chemically different from the polymer in solution initially as stabiliser and this means that the process is only applicable to the production of products including chemically different polymer types. The polymer that was initially in solution may therefore be detrimental to the action of the polymer formed during the process or, at best, the polymer in solution may not contribute useful performance properties to the product even though it increases the weight of the product. We have conducted experimentation in an attempt at modifying the process by the use of a dissolved polymer of the same chemical type as the polymer formed during the process and have confirmed that the polymerisation process is then inoperable and that, at best, a viscous solution is obtained. Accordingly the process described in US Patent Specification 4,380,600 is of very limited applicability as regards the materials that it it can form and use. The production of a high molecular weight polymer having optimum performance characteristics necessitates very careful control of polymerisation conditions and extensive research has been conducted over the years into different types of polymerisation processes, for instance aqueous gel polymerisation and reverse phase bead, suspension or emulsion polymerisation. As a result of this research techniques have been perfected for manufacturing polymers having superior performance properties. The polymerisation process described in US Patent Specification 4,380,600 is necessarily of an entirely new type and it would be unreasonable to expect to be able to perform it regularly in such a way as to obtain high molecular weight polymer having performance characteristics equivalent to those now regularly obtainable by well established commercial gel or reverse phase or other polymerisation processes. Accordingly the products of the process described in US 4,380,600 could not be expected to have performance qualities equivalent to those that are obtainable by other techniques even if a solution had been found to the problem of incorporating a contaminating low molecular weight polymer with the high molecular weight polymer. It is significant that although the patent specification mentions the possibility of using a wide variety of stabilising polymers in practice all the examples except two stabilise the system using solely non-ionic polymer or a blend of non-ionic polymers, generally polyethylene glycol and/or polyvinyl alcohol. The exceptions are Example 5 where 5 grams of polyethylene imine are used with 20 grams of non-ionic polymer to stabilise 40 grams of a monomer mixture including cationic monomer, and Example 9 where 1 gram polysodium acrylate is used with 10 grams non-ionic polymer to stabilise 20 grams of monomer including cationic monomer. Accordingly US Patent Specification 4,380,600 does not contribute to a solution of the existing major problem of providing a high molecular weight water soluble polymer having optimum performance qualities in the form of a fluid product that is free of undesirable or unwanted contaminants. In U.S. 4,525,515 (FR 2,531,093) it is proposed to make a concentrated suspension of water soluble polymer by a method that involves the incorporation of surfactant. The resultant suspension therefore necessarily contains a large amount of surfactant and so will inevitably carry surfactant into aqueous compositions formed from the suspension. This can be undesirable, for instance from an environmental point of view. In U.S. 4,487,866 a process is described in which anionic polymer is rendered more dispersible in water as a result of treatment with, for instance, a cationic polymer and an inorganic salt. The treatment can be conducted in a polar liquid. Methanol and isopropanol are said to be preferred but water is mentioned. The product can then be dried to form a damp solid. None of these proposals meet the desired objective of the provision of an aqueous suspension of a water soluble or water swellable polymer that is stable and that, when used, does not carry unwanted material, in particular surfactant, into the environment. In the invention a water miscible, stable fluid product comprises aqueous gel particles of high molecular weight water soluble polymer having a size of at least 20 µm and interconnected by a continuous phase that is an aqueous solution of an equilibrating agent that holds the water content of the particles in the fluid product in equilibrium with the water content of the aqueous phase and that prevents substantial agglomeration of the particles in the fluid product. The concentration of equilibrating agent in the aqueous solution is 10 to 70% by weight, the ratio (dry weight) of high molecular weight polymer to equilibrating agent is from 1:0.2 to 1:10, the ratio (by weight) of the aqueous solution to gel particles is from 0.5:1 to 10:1 and the gel polymer and equilibrating agent are selected from the combinations of gel polymer and equilibrating agent consisting of: (a) the gel polymer is an anionic polymer and the equilibrating agent is selected from water soluble anionic polymer of ethylenically unsaturated monomers, blends of water soluble cationic polymers of ethylenically unsaturated monomers with inorganic salts, and polydiallyldimethyl ammonium chloride; (b) the gel polymer is a cationic polymer and the equilibrating agent is selected from water soluble cationic polymers of ethylenically unsaturated monomers, polyethylene imine polydimethylamine epichlorhydrin and blends of water soluble anionic polymers of ethylenically unsaturated monomers with inorganic salts; (c) the gel polymer is a non-ionic polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers or a water soluble cationic polymer of ethylenically unsaturated monomers; and (d) the gel polymer is a cellulosic or starch polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers. The product is best made by dispersing into the aqueous medium polymer particles that may either be aqueous polymer particles having a size greater than 20 µm or dry polymer particles that will absorb water from the aqueous medium to form aqueous gel particles greater than 20 microns. In the prior art dispersions of water soluble polymers required the provision of a continuous oil phase interconnecting the particles and a surfactant to assist in dispersion of the particles into the oil or a surfactant to assist in dispersion of the oil into the water in which the particles are subsequently used, or both. In the invention the need to use oil is avoided and the need to use the undesirable surfactants that were previously essential is also avoided. Instead the continuous, interconnecting, phase is merely an aqueous solution of an equilibrating agent which, as explained below, can be selected from a wide variety of materials so that, for any particular use, the composition can be formulated from materials that are acceptable and, in some instance, the equilibrating agent can be selected so as to improve the properties of the dispersed polymer. The fluid product of the invention can be referred to as a dispersion but it should be understood that the particles are not generally held suspended in a continuous matrix of the aqueous phase but instead generally rest substantially in contact with one another but slide over one another. It appears that the aqueous phase provides a film around and between the particles to prevent them aggregating and to permit the composition to be fluid. Thus the product is stable in that upon static storage the particles remain substantially freely movable with respect to each other and if there is any tendency towards aggregation of particles this aggregation can easily be destroyed, and the fluidity of the product restored, by simple stirring or agitation. The product is water miscible in that the individual gel particles can easily be dispersed individually into water, and dissolve, upon simple addition of the fluid composition to the dilution water. Thus there can be little or no tendency for the individual particles to aggregate when the fluid product is added to dilution water. As the product can be regarded as consisting primarily of particles resting substantially in movable contact with one another, rather than a dispersion of particles in excess continuous medium, the normal rules of increasing stability by reducing particle size may not apply. Instead of desiring the smallest possible particle size, as is required in conventional dispersions, in the invention it is preferred that the average particle size in the dispersion should be above 50 µm and preferably above 100 µm. Best results are generally obtained when the average particle size is in the range 200 µm to 2 mm, often 500 µm to 1 mm, but the particle size can be as large as, for instance, 3 or even 5 mm. In U.S. 4,380,600 it is clear that the dispersion of microscopic particles stabilised during the formation of the particles by polymerisation and it is also clear, as discussed above, that the mechanism is of very limited applicability as regards combinations of polymers. It is very surprising that in the invention it is possible to obtain a fluid stable composition from much larger particles and that the continuous phase for this should be an aqueous solution of an equilibrating agent that in practice is generally selected from materials entirely different from those specifically proposed in U.S. 4,380,600. It is also very surprising that when dispersing a water soluble polymer in an aqueous phase it is possible to obtain a stable composition of the gel particles within the aqueous phase, without the aqueous phase dissolving the gel particles so as to form a sticky mass or homogeneous gel. It is of course known that aqueous gel particles can be dispersed in oils or in hydrophilic liquids such as methanol or polyhydric alcohols. However all such materials incur disadvantages in the production or use of the compositions. Forming dispersions in, for instance, methanol necessitates handling large quantities of a highly flammable material. Forming dispersions in polyhydric alcohol necessitates handling difficulties and can result in cross linking or otherwise undesirable modification of the surface properties of many polymers. If the continuous phase is, initially, a substantially non-aqueous organic liquid it is inevitable that large amounts of this non-aqueous liquid have to be used and so can pollute water into which the compositions may eventually be discharged. As a result of using an aqueous solution as the continuous phase the amount of organic or other component in the continuous phase is reduced so that pollution problems are reduced and the toxicity, flammability and reactivity problems of, for instance, methanol and polyhydric alcohols are avoided. One preferred way of making the products of the invention, and of carrying out the method of the invention, comprises adding substantially dry particles of the high molecular weight water soluble polymer to the aqueous solution of equilibrating agent, whereupon these particles will absorb water and become gel particles as a result of equilibration between the water content of the continuous phase and the water content of the gel particles (the two final water contents generally being different). The dry particles added in this manner will generally hava a water content below 20%, typically 3 to 10%, and will generally have a particle size of from 10 µm to 2 mm, generally 100 µm to 1 mm. The dry particles swell as they absorb water and will generally have a final particle size in the fluid product of from 50 µm to 10 mm, generally 500 µm to 5 mm. Alternatively the high molecular weight polymer can be introduced in the form of gel, for instance having a water content (based on water plus polymer) of at least 50% and generally 60 to 80%. The water content of the gel particles may be at a level such that there is substantially no transfer of water into or out of the particles when they are added to the aqueous solution or their water content may increase or decrease after addition, as a result of the transfer necessary to achieve equilibrium between the water contents of the aqueous solution and the gel particles. The gel may be added in the form of particles having the desired particle size (for instance a particle size of 500 microns to 5 mm) or may be added as larger pieces that must be comminuted after they have been added to the aqueous solution. The pieces may be blocks having a size of 500 mm or more and may be comminuted by being forced with the aqueous medium through an extruder and chopper, or may be granules, for instance fragments obtained by cutting a block of gel into pieces. The granules may have a particle size of, for instance, 3 to 200 mm or more, typically 5 to 100 mm. A blend of the granules and the medium may be milled by passage through any convenient apparatus for milling aqueous dispersions. A suitable apparatus is an in-line Silverson mixer, the milling may be effected in a single pass through the mixer or the blend may be passed through two or more mixers in series or through one mixer two or more times, the conditions being selected to give the desired final gel particle size. Similarly, if the polymer is initially introduced substantially dry but with a particle size larger than is desired it is possible to mill, in the same manner, the fluid product existing after the polymer particles have become aqueous gel particles as a result of wholly or partially equilibrating with the aqueous phase. The polymer that is added to the aqueous phase may have been formed by any convenient method capable of producing polymer having the desired performance characteristics and having particulate or other suitable physical form. For instance dry particles may have been made by reverse phase bead or other polymerisation processes followed by drying the resultant dispersion and separating the dry particles from the non-aqueous liquid or they may have been made by gel polymerisation followed by drying and comminuting the gel. Gel particles are generally fragments obtained by comminution of a mass of rigid aqueous gel, for instance as obtained by bulk aqueous gel polymerisation. This fragmentisation may be conducted in conventional manner, for instance by cutting a mass of gel into pieces and/or by extruding a mass of gel through coarse orifices, optionally cutting the gel before or after the extrusion. Other ways of making the starting polymer particles include precipitation polymerisation, emulsion or dispersion polymerisation with coagulation and optionally drying, and spray drying a polymer emulsion or dispersion. Gel that is to be comminuted before or after contact with the aqueous medium must be sufficiently rigid that it can be comminuted into discrete particles without risk of these particles flowing into one another. Generally it has characteristics typical of gels that are air comminuted at present. Normally the viscosity of the gel is above 200 Pa·s at 25°C. The dry or gel polymer may consist only of the high molecular weight polymer and any water that is present or the polymer may be mixed with other components, for instance inorganic salts as described in European Patent Application No. 84302555.2. The high molecular weight polymers are formed from water soluble monomers or water soluble blends of monomers by gel polymerisation or by any other convenient way of making soluble polymers. They normally have a molecular weight above 0.5 million, preferably above 1 million, for instance 5 to 30 million. They are useful as, for instance, viscosifiers and flocculants. The equilibrating agent used in the invention acts by equilibrating the water content of the gel particles with the water content of the aqueous solution at a value such that the gel particles remain as separate particles and do not dissolve or agglomerate. In the absence of an appropriate amount of equilibrating agent the gel particles would absorb water from the aqueous solution to such an extent that they would either become so soft and sticky at their outer surfaces that they would agglomerate or they would fully dissolve. The equilibrating agent prevents the particles taking up this amount of water and instead holds the water content of the particles in equilibrium with the surrounding aqueous solution. If the particles are introduced having the equilibrium content then the equilibrating agent will prevent any substantial net transfer of water into or out of the particles, but in most instances the particles are introduced having a water content different from the desired final water content, in which event the equilibrating agent permits net transfer of water into or out of the particles until they achieve equilibrium, whereafter there is no further substantial net transfer of water into or out of the particles. The choice of equilibrating agent is determined by the nature of the polymer. A phenomenon similar to osmosis may be utilised in the invention since if the ionic concentration in the aqueous medium is appropriate having regard to the ionic concentration of the gel granules or particles there may be little or no tendency for water to transfer from one phase to the other. However the polymer particles will have an inherent tendency to attract water, for instance by hydrogen bonding, irrespective of the ionic state and so the equilibrating agent may not be capable of being selected solely on the basis of conventional osmosis considerations. For instance although it is known that certain inorganic salts can be used in high concentrations to dehydrate aqueous gels, in the invention salt can be used with the polymer. The preferred combinations of gel polymer and equilibrating agent are those that do not involve inorganic salt and thus are combinations of anionic gel polymer and equilibrating agent that is a water soluble anionic polymer of ethylenically unsaturated monomers, cationic gel polymer and equilibrating agent that is water soluble cationic polymer of ethylenically unsaturated monomers, polyethylene imine or dimethylamine epichlorhydrin reaction product, and combinations (c) and (d). However dissolved inorganic salt can be present. This water soluble salt may be introduced as a component of the gel, with consequential leaching from the gel particles into the aqueous medium, but often is deliberately added to the aqueous medium with the water soluble polymer, separate from the gel particles. If the gel polymer is ionic the dissolved equilibrating agent preferably is co-ionic but in some instances may be counter-ionic, especially if inorganic salts is included in the equilibrating agent. The inclusion of inorganic salt can reduce the amount of co-ionic polymer in solution that is required to give appropriate equilibration. Any salt or other equilibrating agent should be chemically inert during the process. For instance it should not undergo unwanted hydrolysis. Generally non-ionic equilibrating agents are not very satisfactory for use with ionic polymers. If the high molecular weight polymer is non-ionic, especially polyacrylamide, cellulosic or starch polymers then the equilibrating agent can be selected from anionic, and cationic materials. In one preferred product the high molecular weight polymer is anionic and the equilibrating agent comprises dissolved anionic polymer. In another preferred product the equilibrating agent is polydiallyl dimethyl ammonium-chloride, the high molecular weight polymer preferably being cationic. In another preferred product the equilibrating agent comprises a dissolved ionic polymer in an amount of at least 0.3 and generally at least 0.5 parts per part dry weight of the high molecular weight polymer. In another preferred product the equilibrating agent comprises a dissolved polymer formed from at least one monomer that is the same as a monomer from which the high molecular weight polymer is formed, the equilibrating polymer and high molecular weight polymer preferably being homopolymers of the same monomer or copolymers formed from the same monomers, either in the same or different proportions. In addition to selecting an appropriate material or mixture of materials for use as the equilibrating agent it is also necessary to select an amount of these materials to provide the desired effect. For instance if appropriate equilibration is obtained at one concentration of the chosen material or blend of materials it will be found that upon reducing this concentration sufficiently equilibration will be lost and a viscous solution or rubbery mass of gel particles will be obtained, instead of the desired discrete rigid gel particles. The initial aqueous solution of equilibrating agent should have low viscosity and in particular will generally have a viscosity below 20 Pa·s at 25°C, most preferably below 10 Pa·s at 25°C, and so the equilibrating agent should not cause a substantial increase in the viscosity of the aqueous medium. Any polymer that is dissolved in the aqueous medium must therefore be of relatively low molecular weight, and will generally have a molecular weight below 500,000, often below 100,000, if cationic or non-ionic. Anionic dissolved polymers should normally have a molecular weight below 20,000 and preferably below 10,000, and most preferably below 5,000. Suitable anionic gel polymers that can be utilised in the invention are water soluble or swellable salts of polymers of acrylic acid, methacrylic acid or acrylamido methyl propane sulphonic acid (AMPS) or other ethylenically unsaturated carboxylic or sulphonic acids optionally copolymerised with each other or with non-ionic ethylenically unsaturated, generally acrylic, monomers such as acrylamide. With such polymers the preferred equilibrating agents are water soluble anionic polymers, preferably homopolymers such as sodium acrylate or acrylamido methyl propane sulphonic acid (AMPS) sodium salt or other salts or other anionic monomer, and copolymers with monomers that do not render the polymer ineffective. Particularly preferred novel products according to the invention are therefore the defined fluid products in which the gel polymer is one of the anionic polymers or copolymers discussed above and the equilibrating agent is a water soluble anionic polymer, preferably a polymer of sodium acrylate or AMPS sodium salt. Particularly preferred products are those in which the dispersed polymer is a sodium or other appropriate salt of acrylic acid, optionally copolymerised with acrylamide and the equilibrating agent comprises low molecular weight sodium acrylate, typically as an aqueous solution of 15 to 55%, preferably 30 to 45% by weight. Instead of using the dissolved polymer alone, the required concentration can be reduced by the addition of inorganic salt such as sodium sulphate. Some cationic polymers can be used as equilibrating agent for the dispersed anionic polymers, especially in the presence of an inorganic salt, for instance poly-diallyldimethyl ammonium chloride (poly-DADMAC), typically as an aqueous solution of 10 to 50%, preferably 15 to 30%, by weight, and polyvinyl pyridine salts. Non-ionic polymers are generally found to be ineffective with dispersed anionic polymers. Suitable dispersed cationic polymers that can be used in the invention are polymers of DADMAC, vinyl pyridine methacrylamidopropyl trimethylammonium chloride (MAPTAC) and dimethylaminopropyl methacrylamide (DMAPMA) acid salts but, most preferably, are salts or quatemary salts of dialkylaminoalkyl-methacrylates, -acrylates or -acrylamides, optionally copolymerised with other acrylic or ethylenically unsaturated monomers, generally non-ionic monomers such as acrylamide. Suitable equilibrating agents for these cationic polymers include dissolved cationic polymers such as poly-DADMAC (this giving particularly valuable final products) or other quaternary polymeric salts, polyvinyl pyridine salts, polyethylene imines and certain anionic polymers, especially when mixed with salt. Non-ionic polymers are again generally unsatisfactory. The preferred dispersed non-ionic polymer that is used in the invention is polyacrylamide but others that can be used include polyvinyl pyrrolidone, hydrolysed polyvinyl acetate and N-vinyl N-methyl acetamide or formamide. As equilibrating agents there are preferably used a variety of dissolved anionic polymers such as those discussed above, for instance sodium pdlyacrylate, or cationic polymers, for instance poly DADMAC. Generally there is no advantage in including an inorganic salt when stabilising a dispersed non-ionic polymer. All synthetic polymers used in the invention are preferably formed from ethylenically unsaturated monomers, preferably acrylic. The dispersed polymers can be natural or modified products, instead of the synthetic polymers discussed above. For instance they can be non-ionic or anionic and can be cellulose derivatives such as methyl cellulose or hydroxy ethyl cellulose or sodium carboxymethyl cellulose. Starch derivatives may be used, for instance a starch acrylamide and/or sodium acrylate product. For these products the preferred equilibrating agents are dissolved anionic polymers, particularly sodium acrylate. Blends of polymers may be used as equilibrating agent, any blend preferably being co-ionic. Thus a blend of anionic polymers or of cationic polymers. If salt is used as part of the equilibrating agent the amount is generally from 0.3 to 5, most preferably 0.5 to 2, parts by weight per part by weight dissolved polymer. If the equilibrating agent can either be a dissolved polymer by itself or a blend of that dissolved polymer with salt the amount of salt used in the blend is generally from 1 to 3 parts, generally abut 2 parts, by weight salt per part by weight of the dissolved polymer that is replaced by the salt. For instance if the equilibrating agent can conveniently be 100 grams dissolved polymer similar results may be obtainable with 50 grams dissolved polymer and 100 grams of the salt. If inorganic salt is used it is usually an alkali metal or ammonium salt, often a sulphate or halide. The preferred material is sodium sulphate but others that may be used include ammonium and sodium chloride. In general any material that will ionise in the aqueous medium can be used provided it does not deleteriously affect the gel polymer or any solution polymer in the dispersion and provided it is commercially acceptable in the final product. The concentration of dissolved equilibrating agent in the aqueous solution will be above 10% by weight but below 70% and usually below 60%. If used by itself the amount of dissolved polymer is generally at least 20%, and usually at least 30%, for instance up to 50%, by weight of the aqueous medium but if used as a blend with a salt it may be less, for instance at least 15% by weight of the medium. The amount of the salt, if present, is generally at least 5%, typically 15 to 30%, by weight of the medium. The ratio by dry weight of high molecular weight polymer to equilibrating agent is from 1:0.2 to 1:10, most preferably 1:0.3 to 1:4, these values being particularly applicable when the equilibrating agent consists of dissolved polymer. The amount is usually at least 0.5 parts. The amount of aqueous medium is usually at least 0.5, and generally at least one part by weight per part by weight of aqueous gel (i.e., based on the weight of polymer and water in gel particles) but is normally below 10 parts. Amounts of from 1.2 to 5, preferably around 2, parts by weight aqueous medium per part by weight aqueous gel are often preferred. Expressed alternatively, the amount of aqueous medium is generally 1.5 to 30, preferably 3.6 to 15, parts by weight per part dry weight of polymer in the gel. The aqueous solution used for forming the fluid products of the invention should provide sufficient water to permit the dispersed particles to have the equilibrium water content but preferably does not provide a substantial excess of water over this. Generally the total amount of water (including both the water introduced in the aqueous solution and any water introduced in the polymer particles) is from 0.5 to 10, most preferably 0.9 to 5, parts water per part dry weight of dispersed polymer. If excess water is present the fluid product may separate into two layers, one layer being a fluid layer comprising the aqueous gel particles interconnected by the continuous phase and the other layer comprising aqueous solution of equilibrating agent. Since water is generally transferred between the aqueous solution of equilibrating agent and the polymer particles it follows that the water content of the continuous phase that interconnects the particles may be different from the water content of the initial aqueous solution (unless the transfer of water is accompanied by a corresponding transfer of equilibrating agent into or onto the particles). It appears that the transfer of water, especially transfer into the particles, results in the accumulation of a concentration of equilibrating agent on or adjacent to the surfaces of the particles. The existence of this area of concentration equilibrating agent may be important to success in the invention, for instance as a result of providing a lubricant film into which the gel polymer particles cannot dissolve but which prevents agglomeration and facilitates slippage of the adjacent particles over one another. This film may be a concentrated solution of the dissolved, water soluble, polymer or other equilibrating agent and so is entirely different from the water insoluble film that may enclose the individual particles of conventional dispersions of soluble polymer. The dry weight of the dispersed particles in the fluid product conveniently is from 3 to 50% but most preferably is generally in the range 15 to 30%. The total dry weight of polymer in the product (i.e. the dry weight of dispersed polymer and any dissolved polymer that serves as equilibrating agent) is generally from 10 to 70% by weight, preferably 30 to 60% by weight. The products of the invention are fluid products in that they flow readily upon their initial formation and that, upon storage, they either flow readily or can be made to flow merely by gentle stirring or other application of shear. The fluidity properties depend upon the combination of gel polymer, equilibrating agent, amounts of these and water, and particle size. The invention provides, for the first time, the possibility of supplying water soluble particulate polymer of chosen performance characteristics in the form of a fluid product that does not contain substantial amounts of unwanted surfactant or unwanted non-aqueous phase. The invention also provides, for the first time, the opportunity of providing such a product free of unwanted or inert dissolved polymer and, in particular, of providing such a product having a substantial amount of a dissolved, generally low molecular weight, polymer in combination with dispersed, generally high molecular weight, polymer. Processes in which mechanical or chemical operations are conducted on gel particles while present in an aqueous medium containing an equilibrating agent are described and claimed EP 0169674. The following examples illustrate the invention. In the examples the proportions are by weight, unless otherwise stated, and I.V. stands for intrinsic viscosity. Example 1 40 g of a 40% aqueous solution of polydiallyldimethyl- ammonium chloride (M w 72,000) was diluted with 40 g of water, as the aqueous solution of equilibrating agent. 20 g of a powdered copolymer of methyl chloride quaternized dimethylaminoethyl acrylate/acrylamide (40/60 w/w ratio-I.V.=11.3 dl g -1 3 M NaCI, 30°C) was added to the solution with gentle agitation. The resultant product was a fluid dispersion which remained stable over a 2 months' period. The process of this example was repeated, with similar results, using the combinations of equilibrating agent and powdered polymer shown in Table 1. SA=sodium polyacrylate. Equilibrating agent Powdered polymer 1 37.5 g 40% DADMAC Mw 72,000 15 g NaCl 42.5 g water 20 g 34/66 SA/ACM (IV 17.0) 2 40 g, SA Mw 3,500, 15 g NaCl 40 g water 20 g 40 QDMAEA · MECL/60 ACM (IV 11.0) 3 100 g 30% ammonium polyacrylate Mw 3,500 30 g Natrosol 250 H 4 100 g 20% SA Mw 3,500 20 g Methocel HB Natrosel is a registered trade mark of Dow Chemical Corporation for hydroxyethyl cellulose and Methocel is a registered trade mark of Hercules Powder Co. for methyl cellulose. Example 2 140 gms of pieces of a rigid aqueous gel polymer of 16/84 w/w sodium polyacrylate/acrylamide (I.V.=15.0) having a polymer concentration of 33% was added to 125 gms solution of a homopolymer of sodium polyacrylate, Mw 3500 and the blend was milled using a 'Silverson' type mixer to produce a fine free flowing dispersion of gel particles. The product remained stable over a 2 months' period. Example 3 The process of Example 2 was repeated with a gel copolymer of 55% by weight sodium acrylate 45% acrylamide (IV 20, 33% solids gel) and aqueous media with the results shown in Table 2. In this Table the following abbreviations are used SA-sodium acrylate polymer SMA-sodium methacrylate polymer ACM-acrylamide polymer PVP-polyvinyl pyrrolidone PEG-polyethylene glycol AMPS-sodium acrylamido-2-methyl propane sulphonic acid PVA-polyvinyl alcohol NVNMA-N-vinyl-N-methyl acetamide polymer DADMAC-diallyl dimethyl ammonium chloride polymer QDMAEMA-quaternised dimethylaminoethyl methacrylate polymer MECl-methyl chloride QDMAEA-quaternised dimethylaminoethyl acrylate polymer DMS-dimethyl sulphate SS-sodium sulphate The proportions of monomers used in the identified copolymers are by weight. The following results were obtained. Samples 3, 4, 8, 10, 14 to 19 and 24 were- unsatisfactory. Aqueous medium Observation of fluid milled dispersion 1 40% SA, Mw 3,500 No swelling 2 30% SA, Mw 3,500 No swelling 3 20% SA, Mw 3,500 Some swelling 4 10% SA, Mw 3,500 Reject-rubbery gel 5 20% SA, Mw 3,500+20% SS No swelling, some crystals 6 20% SA, Mw 3,500+10% SS No swelling, some crystals 7 15% SA, Mw 3,500+20% SS No swelling, some crystals 8 15% SA, Mw 3,500+15% SS Reject-dissolves to form gel 9 40% 20-isobutylmethacrylate/80-SA Mw 4,000 No swelling 10 30% PVP Slight dissolution 12 40% 20-AMPS/80-SA, Mw 3,083 No swelling 13 40% 40-AMPS/60-SA, Mw 4,421 No swelling 14 40% ACM Reject-dissolves 15 40% 20-Methylacrylate/80-SA Reject-dissolves 16 25% PVA Reject-dissolves 17 25% PVA+15% SS Reject-PVA precipitates 18 25% PVA+15% PEG Mw 20,000 Reject-dissolves to form gel 19 30% NVNMA Dissolves on prolonged standing 20 40% SA, Mw 4,120 No swelling 21 40% SA, Mw 1,743 No swelling 22 40% 95 SA, 5 PEG, Mw 20,000 No swelling 23 40% 75 SA, 25 PEG, Mw 20,000 No swelling 24 40% 50 SA, 50 PEG, Mw 20,000 Slight swelling Example 4 The process of Example 2 was repeated but using various gel polymers and aqueous media with the results shown in Table 3. Samples 1, 8, 11,12 were unsatisfactory. Gel polymer Aqueous medium Observation of fluid milled dispersion 1 SA (IV12) 40% SA, Mw 3,500 Gels on prolonged standing 2 SA (IV12) 40% DADMAC, Mw 80,000 No swelling 3 50 AMPS-50 ACM (IV10) 40% SA, Low Mw No swelling 4 50 SMA-50 ACM (IV6) 40% SA, Low Mw No swelling 5 30.6% ACM (IV16) 40% SA, Mw 3,500 No swelling 6 30.6% ACM (IV16) 40% DADMAC, Mw 60,000 No swelling 8 30.6% ACM (IV16) 25% PVA Swells on standing 9 30.6% ACM (IV16) 30% PVP No swelling 10 35% 53 QDMAEA MeCl/47 ACM (IV13) 40% DADMAC, Mw 80.000 No swelling 11 35% 53 QDMAEA MeCl/47 ACM (IV13) 30% QDMAEMA MeCl Slight swelling 12 35% 53 QDMAEA MeCl/47 ACM (IV13) 20% QDMAEA DMS Reject-dissolves 13 32% 4 QDMAEA-MeCl/96 ACM (IV7) 40% DADMAC No swelling 14 35% 20 DADMAC/80 ACM (IV8) Aqueous Polyethyleneimine No swelling 15 50% QDMAEA MeCI (IV6) Aqueous Polydimethylamine epichlorhydrin No swelling 16 35% 30 MAPTAC/70 ACM (IV8) Aqueous DADMAC, Low Mw No swelling 17 35% 30 DMAPMA ½ H 2 SO 4 /70 ACM (IV6) Aqueous DADMAC, Low Mw No swelling Those dispersions shown in Examples 3 and 4 as not swelling thus provided fluid products according to the invention whilst those that were rejected gave products that were unsatisfactory either because of total solution of the gel polymer or because the gel swelled to such an extent that it agglomerated. Example 5 A commercially available sodium acrylate/acrylamide copolymer (34/66 w/w ratio I.V.=17) was sieved into three particle size fractions. 50 g of each fraction was dispersed into 150 g of 26.6% aqueous solution of a homopolymer of sodium polyacrylate Mw 3,500, using a high speed stirrer. The viscosity of the resultant dispersions was measured immediately using a Brookfield viscometer at different spindle speeds. The results are shown in Table 4. Particle size range Viscosity (Pa·s) 1 r.p.m. 10 r.p.m. 100 r.p.m. >250 <500 µm 9 7 5 >125 <250 µm 18 12 7 <125 µm 150 45 18 Unsieved material 23 13 10 As the particle size reduces, so the dispersion viscosity increases. All products exhibited reduced viscosity with increasing shear. On standing the products formed light gels which rapidly thinned with mild agitation. Slight separation also occurred. Example 6 The method outlined in Example 1 was utilized except the low molecular weight polymer (continuous phase) was sodium polyacrylate Mw=3,500 (I) and the high molecular weight polymer (dispersed) was a copolymer of 34/66 w/w sodium polyacrylate/acrylamide (II) I.V.=17.0. Various combinations of amounts were used with the results and the Brookfield viscosity at various spindle speeds of each resultant fluid product was recorded after 2 weeks. Viscosity CPS g I (40% w/w) g II (100%) g H 2 O 1 r.p.m. 10 r.p.m. 100 r.p.m. 70 50 80 14,000 880 156 80 50 70 12,000 1248 236 85 50 65 24,200 960 228 90 50 60 19,000 960 122 95 50 55 10,080 740 218 100 50 50 8,120 860 176 100 52.5 50 8,800 880 202 100 55.0 50 15,600 828 180 100 57.5 50 21,480 1120 224 100 60 50 25,000 1200 250 100 62.5 50 24,240 1012 234 100 6.50 50 19,200 1288 320 From this it will be seen that the products became viscous on standing, the viscosity depending upon proportions of the components, but that upon application of moderate shear they were all converted to low viscosity fluids. Example 7 3 polymer powders, A, B and C were used in this Example having the analysis Dry powder used I.V. dl g -1 A 60/40 w/w QDMAEA/Acm MeCl 12.0 B 40/60 w/w QDMAEA/Acm MeCl 11.3 C 27.6/72.2 w/w QDMAEA/Acm MeCl 6.0 3 aqueous dispersions, A, B and C, were prepared, one from each of the polymers, by dispersing 20 g of the polymer into 80 g of a 20% solution of poly-DADMAC (Mw 72,000). All three dispersions were fluid dispersions of swollen gel particles. Solutions of the powders A, B and C were formed in conventional manner. Solutions were also obtained of the corresponding polymers by mixing dispersions A, B or C with water. A solution of the poly-DADMAC was also obtained in conventional manner. The seven solutions were evaluated on a standard waste stock of 40 g newsprint, 10 g manilla and 5 g corrugated paper. This was disintegrated in 2 litre of water to give a standard waste stock of 2.5% consistency. The stock was diluted to 0.5% d/d solids and one litre aliquots dosed with either 200 g or 400 g ton -1 d/d polymer. The flocculated stock was transferred to a Schopper Reigler Freeness Tester whose back orifice had been blocked. The drainage rate was measured by timing the collection of 500 cm 3 water. The results are in Table 6. Product 200 g (sec) 400 g (sec) - 99 99 DADMAC homopolymer 50 53 Powder C 47 30 Powder B 41 25 Powder A 48 26 Dispersion C 23 14 Dispersion A 29 18 This demonstrates that the DADMAC, homopolymer is neither detrimental nor inert, as is the stabiliser used in each of the examples in US Patent 4,380,600, but is instead beneficial to the properties of the product.

Claims: A water miscible, stable, fluid product comprising aqueous gel particles of a high molecular weight water soluble polymer interconnected by a continuous liquid phase that is an aqueous solution of an equilibrating agent that holds the water content of the paticles in the fluid product in equilibrium with the water content of the aqueous phase and that prevents substantial agglomeration of the particles in the fluid product characterised in that the particles have a size of at least 20 µm and the concentration of equilibrating agent in the aqueous solution is above 10 to below 70% by weight, the ratio (dry weight) of high molecular weight polymer to equilibrating agent is from 1:0.2 to 1:10, the ratio (by weight) of the aqueous solution to gel particles is from 0.5:1 to 10:1 and the gel polymer and equilibrating agent are selected from the combinations of gel polymer and equilibrating agent consisting of: (a) the gel polymer is an anionic polymer and the equilibrating agent is selected from water soluble anionic polymer of ethylenically unsaturated monomers, blends of water soluble cationic polymers of ethylenically unsaturated monomers with inorganic salts, and polydiallyldimethyl ammonium chloride; (b) the gel polymer is a cationic polymer and the equilibrating agent is selected from water soluble cationic polymers of ethylenically unsaturated monomers, polyethylene imine, polydimethylamine epichlorhydrin, and blends of water soluble anionic polymers of ethylenically unsaturated monomers with inorganic salts; (c) the gel polymer is a non-ionic polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers or a water soluble cationic polymer of ethylenically unsaturated monomers; and (d) the gel polymer is a cellulosic or starch polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers. A product according to claim 1 that has been made by dispersing into the aqueous medium polymer particles selected from aqueous gel polymer particles having a size greater than 20 µm and dry particles that will absorb water from the aqueous medium to form aqueous gel particles having a size greater than 20 µm. A product according to claim 1 or claim 2 in which the gel particles are between 100 µm and 2 mm in size. A product according to any preceding claim in which the gel particles are of a high molecular weight water soluble ionic polymer and the equilibrating agent comprises a dissolved ionic polymer in an amount of at least 0.5 parts per part by weight of the high molecular weight polymer and also comprises an inorganic salt when the dissolved ionic polymer is counterionic to the gel polymer. A product according to any preceding claim in which the gel polymer and equilibrating agent are selected from the combinations consisting of (a) the gel polymer is an anionic polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers, (b) the gel polymer is a cationic polymer and the equilibrating agent is a water soluble cationic polymer of ethylenically unsaturated monomers, polyethylene imine, or polydimethylamine epichlorhydrin, product, (c) the gel polymer is a non-ionic polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers or a water soluble cationic polymer of ethylenically unsaturated monomers, and (d) the polymer is a cellulosic or starch polymer and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers. A product according to claim 5 in which the gel polymer is an ionic polymer and the equilibrating agent is a co-ionic water soluble polymer, or the gel polymer is a non-ionic polymer. A product according to claim 5 in which the gel polymer is anionic and the equilibrating agent is present in an amount of at least 0.3 parts per part by weight of the gel polymer and is a water soluble anionic polymer of ethylenically unsaturated monomers. A product according to claim 5 in which the gel polymer is selected from the group consisting of polyacrylamide, cellulosic and starch polymers and the equilibrating agent is a water soluble anionic polymer of ethylenically unsaturated monomers and the amount of equlibrating agent is at least 0.3 parts per part dry weight of the gel polymer. A product according to claim 5 in which the gel polymer is an anionic polymer of ethylenically unsaturated monomers comprising sodium acrylate and the equilibrating agent is selected from the group consisting of water soluble sodium polyacrylate having molecular weight below 10,000 and blends of 1 part polydiallyldimethyl ammonium chloride with 0.3 to 5 parts inorganic salt. A product according to claim 5 in which the gel polymer is a cationic polymer of ethylenically unsaturated monomers and the equilibrating agent is selected from the group consisting of water soluble polydiallyldimethyl ammonium chloride, quatemised dialkylaminoalkyl (meth) acrylate and polyethylene imine. A product according to claim 5 in which the aqueous medium is a solution of 15 to 55% by weight sodium polyacrylate and the gel polymer is a polymer of sodium acrylate optionally copolymerised with one or more non-ionic or anionic monomers. A product according to claim 5 in which the aqueous medium is a solution of 10 to 50% by weight diallyldimethyl ammonium chloride and the gel polymer is selected from polymers and copolymers of dialkylaminoalkyl -acrylates and -methacrylates and acid addition and quaternary ammonium salts thereof. A product according to any preceding claim 1 in which the total amount of water in the product is 0.9 to 5 parts per part dry weight gel polymer, the ratio by weight gel polymer to equilibrating agent is 1:0.3 to 1:4 and the total weight of gel polymer and dissolved polymer is 30 to 60% by weight of the product.

Inventors: FARRAR DAVID, FLESHER PETER, FARRAR, DAVID, FLESHER, PETER
Applicants: ALLIED COLLOIDS LTD, ALLIED COLLOIDS LIMITED
Application year: 1985
Main classification: C08J3
IPC codes: D06M15, C08J3, D21H17, D06M13, D21H19, C02F1, B01D21, B01J13