COMPOSITION AND PROCESS FOR FORMING INORGANIC RESINS

Abstract: Inorganic resins are formed by mixing: (a) a liquid component A comprising an aqueous solution of one or both of mono aluminum phosphate and mono magnesium phosphate, the solution having a viscosity of from 700 to 10,000 centipoises; and (b) a liquid component B comprising an aqueous vehicle, a phosphate-reactive constituent which is one or both of wollastonite and magnesium oxide, and a non-­ reactive dispersing agent, component B having a viscosity permitting it to be rapidly and thoroughly mixed with component A so as to form a slurry which reacts exothermic­ ally to form an inorganic resin. Such inorganic resins may be obtained in non-cellular or cellular form.

Description: Composition and process for forming inorganic resins This invention is concerned with compositions and processes for forming inorganic resins and articles of manufacture including such inorganic resins disposed on a support surface and, more particularly, to inorganic resin cements having a unique combination of properties and E wide range of uses. The inorganic resin cements of the present invention may be formed as noncellular structures. A number of inorganic resin cement systems are known. Some are formed of magnesium oxychlorides or magnesium oxysulfates (U.S. Patents 3,320,077; 4,141,744; and 4,315,967); and others are formed using phosphates and magnesia. Exemplary of this latter type are compositions of an acid magnesium phosphate, magnesia, silica1 mineral fibers and water in an amount from 70 to 140% of the weight of the remaining components (U.S. Patent 3,752,684); compositions in which a low reactivity magnesia is reacted with an acid aluminum phosphate complex containing an anion of a mineral acid (other than an oxyphosphorus acid) or of a carboxylic acid (U.S. Patent 3,923,534); and compositions formed of a solution of an acid and aluminum phosphate (e.g., Al(P04)3) slurried with silica, alumina and magnesia (U.S. Patent 3,991,254). The insulating materials of U.S. Patent 3,752,684 require the removal of large amounts of water at elevated temperatures; the cold setting refractory materials of U.S. Patent 3,923,534 require extended periods (e.g., 6-8 hours) to set and the slurries used to form the insulating structures of U.S. Patent 3,991,254 must be fired at 5000C or above. Finally, mono-ammonium and diammonium phosphates have been reacted with dead-burned magnesium oxide. These compositions have a number of inherent disadvantages, among which are intense ammonia odor and the formation on top of the resulting cements of a phosphate solution residue. Generally, such prior art inorganic resin systems using phosphates and magnesia have been of a character which has limited their uses to such applications as refractory linings, thermal insulation and use in preparing fast-setting, bonded aggregate structures as replacements for cements and mortars. We have now found that inorganic resins can be formed by an exothermic reaction between one or both of mono aluminum phosphate and mono magnesium phosphate, and one or both of wollastonite and magnesium oxide. The rapid exothermic reaction drives off any water in the liquid reaction mixture without the use of externally applied heat. Further, the use of relatively inexpensive materials compared to typical organic resins offers a number of advantages over many of the organic resins destined for similar applications. The inorganic resins of the present invention can be formulated to be essentially nonflammable, strong and resistant to water and most chemicals including acids, alkalies and organic solvents. The inorganic resins of the present invention can replace at least a portion of the presently known organic resins in a wide range of applications, for example molded configurations (in cellular and noncellular structures); thermal, electrical and/or acoustical insulations; binders and adhesives; coatings and or surfacing agents; patching compositions, man-made boards including organic, for example cellulosic, fibers and/or inorganic fibers, such as fiberglass and the like. According to the present invention, there is provided a two-component system for mixing to form an inorganic resin, which comprises: (a) a liquid component A comprising an aqueous solution of one or both of mono aluminum phosphate and mono magnesium phosphate, the solution having a viscosity of from 700 to 10,000 centipoises; and (b) a liquid component B comprising an aqueous vehicle, a phosphate-reactive constituent which is one or both of wollastonite and magnesium oxide1 and a non-reactive dispersing agent, component B having a viscosity permitting it to be rapidly and thoroughly mixed with component A so as to form a slurry which reacts exothermically to form an inorganic resin. Anuireactive low-water demand filler1 e.g., silica1 milled fibers or a preformed cellular material may, if desired, be added to component A. Wollastonite also may be added to component A to give the resin added resistance to cracking. The resin may be made in cellular form by adding a blowing agent, preferably calcium carbonate, to component B and a surfactant to either or both components. The two liquid components A and B are mixed to form a reactive inorganic resin cement mixture immediately prior to applying the resin mixture on to a resin cement support surface. Component B should have a viscosity permitting it to be rapidly and thoroughly mixed with component A, for example 700 to 10,000 centipoises, and components A and B are mixed to form a slurry and react exothermically to set up as an inorganic resin. Set up times, once the two liquid components are mixed, range from 30 seconds to several minutes. The two liquid components can be mixed in a continuous mixing head to form the resin cement mixtures as the mixture is sprayed from the mixing head toward a resin cement support surface. The resin cement support surface can be any surface capable of supporting the resin cement surface during set-up, for example, a fiberglass mat or a rigid mold. The two liquid components form a reactive slurry and the reaction begins upon mixing and continues exothermically during set-up and curing driving away any water in the mixture without the need for any externally applied heat. The resin is completely cured without any externally applied heat within a period ranging from several hours to several days. The phosphate reactive constituent of component B may be reactive wollastonite, defined herein as wollastonite having an aspect ratio less than about 10:1, magnesium oxide having a relatively low surface area for example, dead-burned magnesium oxide or any other magnesium oxide having a surface area in the range of 0.1 mê/gm to 5 mê/gm; or mixtures thereof. The inorganic resins formed by reaction between components A and B are characterised by good strength; nonflammability; resistance to heat, chemicals, including water, and ultra-violet radiation; and by their adaptability to being formed into structural configurations. The resin may also include fillers, such as silica, milled fibers, preformed cellular materials, and the like, as well as non-reactive wollastonite, defined as wollastonite having an aspect ratio of at least 15:1. These additives contribute to the various desired properties of the resin. Finally, the resins may be cellular in form, the preferred size of the cells ranging from ultrafine to medium. The inorganic resins of this invention are formed by providing two separate liquid components capable of extended shelf life when separated and immediate reaction which when mixed to form the resin. The reaction is exothermic and no additional heat is required to accomplish resin set-up and final cure. The quantity of water in the mixture of components should be maintained at a low level, for example less than 40 of the total weight of the mixture, and preferably less than 25% of the total mixture weight, to minimize the amount which must be removed during curing. The total water in the mixture is preferably less than 3096 of the total weight of components A and B to increase resin stability and integrity while permitting set-up times ranging from as little as 30 seconds to several (for example, 15) minutes and cure times of the order of a few hours to a few days. The resins may be formed with or without cells and include a unique combination of properties including high strength; good thermal, electrical and acoustical insulative properties; chemical and moisture resistance; nonflammability and nonsmoking. The structure of the cellular forms may be varied to provide materials of varying densities. The viscosities of the two liquid components are preferably from 700 to 10,000 centipoises at 25 0C and they are preferably matched, i.e. - 25%, in viscosities to permit rapid and thorough mixing of the components. The ensuing reaction upon mixing is exothermic and rapid. The liquid times, set-up times, and foaming times, as well as the physical properties and physical forms of the resin can be predetermined through the addition of various constituents to the two components. This will be made apparent from the following detailed description of thw two liquid components and the examples. To achieve the full advantage of the present invention the amount of water in each components A and B should, as already stated, be minimized provided the two components are pourable and easily mixable liquids. Excess water1 for example more than about 40% based on the total weight of components A and B, may result in shrinking and cracking, steam explosion, and/or bond rupturing in the resins during setting and curing as well as during any subsequent use of the resins at elevated temperatures. The exothermic reaction of components A and B provides a controlled source of energy sufficient to remove any water from the mixture while maintaining the structure of the resin. Resin configurations, e.g., sheets, bricks, panels, molded and extruded structures and the like can be formed within minutes without any additional energy input. These configurations exhibit good dimensional stability, remaining essentially unchanged during their subsequent use. The reactive wollastonite used in component B reacts rapidly with mono magnesium phosphate and/or mono aluminum phosphate to form an inorganic resin cement, while being relatively non-reactive with phosphoric acid or other acid phosphate salts. This unexpected reaction between wollastonite and mono aluminum phosphate or mono magnesium phosphate permits the use of 0+ to 100-evS reactive wollastonite as the phosphate reactive constituent in component B, the remainder of the phosphate reactive constituent, if any, being magnesium oxide. The nature of components A and B and preferred features thereof will now be described in greater detail. Component A The mono aluminum phosphate and mono magnesium phosphate of component A are preferably supplied in the form of clear syrupy aqueous solutions, the water in the solutions providing the liquid vehicle for component A to have a viscosity of from 700 to 10,000 centipoises at 25 0C. Exemplary of a suitable mono aluminum phosphate solution is one analyzing 8% Al203 and 33.7% P205, (solids concentration of 50 weight %) and having a specific gravity of 1.47, a pH of 1.0 and a Baume value of 47.50. Exemplary of a suitable mono magnesium phosphate solution is one analyzing 5.3% MgO and 32.6% P205, (solids concentration of 44 weight 50) and having a specific gravity of 1.38, a pH of 1.2 (15' solution) and a Baume value of 42.90. The amount of aqueous mono aluminum phosphate and/or mono magnesium phosphate solution in component A is preferably from 20% to 70,00, by weight of the total weight of components A and B, when mixed. The amount of phosphate constituent (solid basis) is preferably from 10% to 35% by total weight of components A and B. Generally, the use of mono aluminum phosphate is preferred over mono magnesium phosphate for forming cellular resins when a chemical blowing agent is used since the resulting resins exhibit somewhat better high temperature resistance. On the other hand, mono magnesium phosphate generally forms resins having greater strength. A mixture of the two phosphate constituents provides resins having a desired combination of strength and high temperature resistance. One or more inert, low water-demand fillers may be added to component A to form inorganic resins having various physical characteristics. To achieve the full advantage of the present invention, the fillers require no more than about 30 cc water to make a flowable paste of 100 gm of filler. Exemplary of suitable fillers are silica (minus 325-mesh), mineral or glass milled fibers, powdered glass, glass beads, flint, titania, some clays, and varytes, as well as mixtures of two or more of these. The filler may be present in an amount up to 50% by weight of the total weight of components A and B, the amount being determined by such factors as water demand, component viscosity required, and physical characteristics desired of the final inorganic resins. If it is desired to form a syntactic cellular structure, that is one incorporating preformed cellular fillers, then such fillers may be added to component A. A number of different types of such preformed cellular fillers are available, including glass, ceramic or synthetic organic resin bubles, and vermiculite. The cellular filler also should not require more than about 30 cc water to make a flowable paste of 100 gm of filler. The amount of cellular filler to be added will depend upon the cellular structure desired in the final resin and may depend upon the final viscosity of component A needed for compatibility with component B. The total amount of all types of fillers added is preferably up to 50% by weight of the total weight of components A and B. In some resin formulations, particularly those having a cellular structure formed by a blowing or foaming agent, wollastonite in a form which is substantially unreactive is added to the mono aluminum phosphate and/or mono magnesium phosphate of component A. A typical less reactive form of wollastonite useful in accordance with this embodiment of the present invention is a finely divided acicular material having an aspect ratio of at least 15 to 1 and a surface area of less than 1.0 mê/gm. It is a naturally occurring mineral which is essentially pure calcium metasilicate, CaSiO3, having a molecular weight of 116. Surprisingly, the addition of the less reactive wollastonite to component A reduces cracks and shrinkage in the inorganic resins formed. The less reactive wollastonite, when added to component A in accordance with this embodiment of the present invention, is preferably added in an amount up to 10 , and more preferably up to 5%, by total weight of components A and B. To achieve an exceptionally long storage life of component A, the less reactive wollastonite fibers of component A should be added shortly before components A and B are mixed to prevent any premature reaction of the wollastonite fibers with the mono aluminum or mono magnesium phosphate, since even the less reactive wollastonite, as defined herein, reacts with the phosphate. The liquid component A preferably includes a water-repellant surfactant in an amount of from 0.2% to 5% by total weight of components A and B, when a blowing agent is included to form the inorganic resins in cellular form. This surfactant stabilizes the foam during formation and set-up and controls the cell size and density of the final cellular resin. The surfactant is preferably a non-carbonizing surfactant, such as hydrophobic fumed silica1 silicone or a titanate, to prevent formation of carbon within the resin during set-up and curing. If carbonization can be tolerated, surfactants such as calcium, zinc or aluminum stearate may be used. A small amount of such water-repellent surfactants may be added to component A or B or both in formulating non-cellular structures, as well as cellular structures. It may be desirable to control and predetermine the profile of water release from the resin of the present invention during cure and subsequent heating of the resins for particular resin uses. Water release can be controlled by replacing all or part of the inert, low water-demand filler, such as silica, with a chemically hydrated, water-releasing material, such as finely divided hydrated alumina, Al203 .3H20. The use of such a water-releasing material is illustrated in Example 13. In formulating component A, the aqueous solution of mono aluminum phosphate and/or mono magnesium phosphate is preferably prepared by adding water to the phosphate(s) to provide the predetermined concentration of phosphate reactant in water. This liquid is preferably maintained at a temperature around 150C (about 600F) to prevent overheating during component mixing. The less reactive wollastonite, fillers and surfactants, if any, are added to the liquid and mixed to form a slurry ready for the mixing with component B. Component B Component B provides a phosphate-reactive constituent which may be wollastonite and/or magnesium oxide. The wollastonite of component B is distinguished from that which may be optionally added to component A in that it is of an acicular form having an aspect ratio of 10 or less. The reactive wollastonite of component B preferably has an aspect ratio of less than 8:1 and, more preferably, about 5:1. The surface area of the reactive wollastonite is preferably at least 1.0 m2/gm. 2 and, more preferably, at least 1.25 m /gm. A typical reactive wollastonite useful in accordance with the 2 present invention has a surface area of about 1.55 m /gm. Like the wollastonite of component A, it is essentially pure calcium metasilicate, but unlike the material with the much higher aspect ratio, it is highly reactive with the mono aluminum or mono magnesium phosphate constituent. The use of at least some reactive wollastonite as the phosphate-reactive constituent minimizes cracks and shrinkage in the final resin. The amount of reactive wollastonite in component B is preferably up to 40% by weight of the total weight of components A and B. The magnesium oxide used in component B can be considered to have a relatively low reactivity when compared with so-called reactive magnesium oxides having surface areas of at least 5 mê/gm. The magnesium oxide used preferably has a surface area of less than 2.0 mê/gm, 2 and more preferably 1.0 m /gm. or less. A typical magnesium oxide useful in accordance with the present invention has a surface area of 0.75 mê/gm. and is classified as high density, low reactivity magnesium oxide. The magnesium oxide is preferably finely ground and sized to pass a 325-mesh screen. The amount of this magnesium oxide in component B is preferably up to 50 vo by weight of the total weight of components A and B. In general, the more magnesium oxide added1 the more reactive is the mixture and the shorter is the resin set time. The addition of some magnesium oxide imparts added strength to the final resin. When both wollastonite and magnesium oxide are used as the phosphate-reactive constituent in component B, the relative amounts of these reactants may extend over the entire range of from O&commat;F 0+ to 100-%. The weight ratio of phosphate solution of component A to phosphate-reactive constituent of component B is preferably from 50/50 to 65/35, and more preferably from 55/45 to 60/40, for example 58/42. This in turn means that the ratio of phosphate on a dry basis/phosphate reactive constituent is preferably from 25/75 to 35/65 with a typical ratio being 29/71. The dispersing agent of component B is an aqueous phosphate dispersant and is preferably sodium hexametaphosphate, sodium tripolyphosphate, sodium acid pyrophosphate, trisodium phosphate, or tripotassium phosphate. The dispersing agent should be essentially unreactive with the other resin components under the conditions of formulation and mixing. When a noncellular resin is formed with mono aluminum phosphate in accordance with one embodiment of the present invention, the dispersing agent is preferably sodium tripolyphosphate, sodium hexametaphosphate, sodium acid pyrophosphate or mixtures of two or more thereof. One or more of these dispersing agents when used with mono aluminum phosphate to form a noncellular resin provides resins with unexpectedly better strength than other non-reactive dispersing agents. The concentration of the dispersing agent in aqueous solution and the amount of such solution are chosen to effect the required dispersing action and to supply the liquid vehicle of component B to the desired viscosity. The optimum amount of any particular dispersing agent may be readily determined for any selected resin composition. As will be seen in Example 11, when a chemical blowing agent, such as calcium carbonate, is used to form a cellular resin, then the dispersing agent must be chosen to maintain the pH of component B below about 10 to permit the release of carbon dioxide. One or more inert, low water-demand fillers of the type added to component A, as described above, may also be added to component B. If such an inert filler is incorporated in both components A and B, then the total quantity added may amount to about 50% by total weight of components A and B. Cellular structures can be formed by using a chemical blowing agent capable of producing a gas during the mixing of components A and B. The blowing agent is added to component B. The blowing agent should be one capable of releasing a gas either by reaction, decomposition or vaporization in the acid slurry formed when components A and B are mixed. Although it is possible to use other inorganic carbonates, for example sodium carbonate and sodium bicarbonate, it is preferred to use calcium carbonate sized to pass a 325-mesh screen. By adjusting the amount of calcium carbonate, it is possible to form cellular inorganic resins having densities of from 10 to 50 pounds/cubic foot (53.4 to 267 kg/m3). The amount of blowing agent added to component B is preferably from 0.2% to 15% more preferably from 0.59; to 6%, by total weight of components A and B. When mono magnesium phosphate is used as the phosphate reactive constituent, dipotassium phosphate, tripotassium phosphate, tripolyphosphate, tetrapotassium phosphate or mixtures of two or more thereof provide inorganic resin cements with strengths which are at least double the strengths achieved with other dispersing agents tested. These particular dispersing agents react with mono aluminum phosphate and are therefore not suitable in formulations where mono aluminum phosphate is at least 10% of the total weight of the phosphate reactive constituent. Cellular resins also can be made using an inert compressed gas, such as carbon dioxide or air, as a physical blowing agent. The physical blowing agent may be introduced into the mixer as cbmponents A and B are mixed or bled into the front of a static mixer when a static mixer is used for mixing. The water-repellant surfactant which may optionally be added to component A, may also be added to component B either in addition to or in place of that added to component A. The total quantity added to components A or B or both should not be more than 5% by total component weight. In formulating component B, the aqueous solution of the dispersing agent provides the liquid vehicle and to it are added, with stirring, the phosphate-reactive constituent (wollastonite and/or magnesium oxide) along with the blowing agent1 if used, and any additional fillers and surfactants. Component B, like component A, is preferably cooled to about 15 C prior to mixing. Extended shelf life for component B can be achieved by formulating component B in dry form and adding water prior to mixing components A and B. Components A and B may be mixed in any type of blender, mixer or mixing head suitable for rapidly and thoroughly blending two slurries of the viscosity range specified. Such mixers include those equipped with blades, continuous mixing heads and static mixers. The viscosity of the slurry mixture rises rapidly and sufficient heat is developed in the ensuing exothermic reaction to vaporize any excess water as steam. By choice of reactants, the time over which the mixture remains liquid may be varied between some 30 seconds to as much as 10 minutes. Likewise, in forming cellular resins1 the "foam rise" time may be adjusted and varied between about one minute and 5 minutes and the "foam set time between about 1.5 and 10 minutes. As noted previously, the water-repellent surfactant stabilizes the cellular resin during foaming and setup, that is, it prevents cell collapse until the resin sets. Complete curing of the resin takes place at ambient temperature and requires a relative short time, for example from several hours to a few days. The liquid mixture of components A and B may, prior to set-up, be formed into any desired configuration by molding, extruding, compression molding and the like. It may be sprayed on to surfaces, coated on surfaces by any suitable technique, and used to form cellular fillings in predefined spaces. Because of its nonflammability, it is particularly suited for wall panellings; because of its resistance to chemicals and moisture it may be used in making pipes, ducts, and the like; and because of its high dielectric properties it may be formed into insulators and the like. It will be appreciated that these are but a few exemplary uses for the inorganic resins of this invention. In order that the invention may be more fully understood, the following examples are given by way of illustration. In the following examples, the amounts of the various constituents are given in parts by weight. The two components were formulated separately in high speed blenders and then mixed or blended in a mechanical mixer. Components A and B were each at about 15.50C (6o0F) when mixing began. The mono aluminum phosphate is an aqueous solution analyzed to contain 8% Awl 203 and 33.7N P205, (solids concentration of 50 weight ,') 47.50 Baume; and the mono magnesium phosphate is an aqueous solution analyzed to contain 5.3% MgO and 32.6% P205, (solids concentration of 44 weight %) 42.90 Baume. The silica filler was -325 mesh and the wollastonite of component A is an acicular material with an aspect 2 ratio of about 20:1 and surface area of 0.88 m /gm. The reactive wollastonite of component B is an acicular material with an aspect ratio of about 5:1 and surface area of 1.55 mê/gm; and the magnesium oxide is a high purity technical grade material processed from magnesium rich brine, -325-mesh and having a surface area of 0.75 2 M /gm. Example 1 Component A Mono magnesium phosphate 100 parts Silica 100 Wollas tonite 15 Component B Tripotassium phosphate 50% solution 25 Magnesium oxide 70 Silicone 1 (e.g. Dow Corning 772, Union Carbide 272) The resulting resin had a modulus of rupture of 750 psi (52.5 kg/cm2) after two hours and 1470 psi (103 kg/cm2) after four days; a 12.6% weight loss and a specific gravity of 1.64 after four days. Example 2 Component A Mono magnesium phosphate 100 parts Silica 100 Component B Tripotassium phosphate 50% solution 35 Wollastonite 49 Magnesium oxide 21 Silicone 1 This resin had a modulus of rupture of 700 psi (49 kg/cmê) after four days. Example 3 Example 2 was repeated using the same component A, but changing the ratio of wollastonite to magnesium oxide in component B from 70/30 of Example 2 to 10/90. The effect of the magnesium oxide on resin strength was shown by the fact that the resin of this example had a modulus of rupture of 700 psi (49 kg/cm2) 2 after two hours and 1470 psi (103 kg/cm ) after four days. Example 4 Component A Mono aluminum phosphate 100 parts Silica 100 Component B Trisodium phosphate 5% solution 30 Wollastonite 35 Magnesium oxide 35 Silicone 1 The resin had a modulus of rupture of 120 psi (8.4 kg/cm2) after two hours and 300 psi (21 kg/cm2) after four days. Example 5 Component A Mono aluminum phosphate 150 parts Silica 150 Wollastonite 23 Hydrophobic fumed silica 10% methanol slurry 2 Component B Sodium tripolyphosphate 10% solution 47 Wollastonite 70 Magnesium oxide 20 Calcium carbonate 5 This formed a cellular resin having a very uniform, fine cell structure and a density of 22.0 pounds/ cubic foot (117 kg/m3), The foam rise time was one minute and foam set time 2i minutes. Example 6 A cellular resin was made using the same component A as in Example 5, but reducing the amount of dispersing agent to 36 parts and replacing the 90 parts of Wollastonite/magnesium oxide with 105 parts of Magnesium oxide. The resin had a very uniform fine cell structure, a density of 23.0 pounds/cubic foot (123 kg/m3), a foam rise time of one minute and a foam set time of 1+ minutes. Example 7 The mono aluminum phosphate of Example 5 was replaced by an equal weight of mono magnesium phosphate to form a cellular resin having a density of 23.0 pounds/ cubic foot (123 kg/m ), a foam rise time of one minute and a foam set time of 1+ minutes. Example 8 The mono aluminum phosphate of Example 5 was replaced by an equal weight of mono magnesium phosphate to form a cellular resin having a density of 23 pounds/ cubic foot (123 kg/m ), a foam rise time of one minute and a foam set time of 18 minutes. Example 9 Using the resin compositions of Examples 5-8 and varying the amount of calcium carbonate blowing agent used from 0.5 to 6.0 parts produced cellular resins having densities ranging from 32 to 10 pounds/cubic foot (171 to 53 kg/m ), respectively. Example 10 Component A Mono aluminum phosphate 150 parts Clay 2 Calcium stearate 6 Component B Sodium tripolyphosphate 10% solution 50 parts Wollastonite 75 Magnesium 20 Calcium carbonate 4 Silicone 1 The resulting cellular resin had uniform, medium sized cells and a density of 25.6 pounds/cubic foot (137 kg/m ). It had a foam rise time of 2 minutes and a foam set time of 7 minutes. Exposure of the cellular resin to temperatures over 5000C caused the calcium stearate to carbonize, smoke and leave a black deposit. Otherwise, the cellular resin retained its strength, nonflammability and other characteristics. Example 11 A series of resin compositions were made up to form cellular resins using the same components A and B as in Examples 5 and 7, except that the amount and type of dispersing agent added to component B were varied. The pH of each component B was measured and its effect on the density of the resulting cellular material noted. The results are tabulated below in Table 1. Table 1 Effect of Component B pH on Cellular Resin Formation Cellular Density, Dispersing Agent pH of lbs/ft3 (kg/m3) in Component B Component B MAP * MAP * Sodium tripoly phosphate (10%) 9.8 22.0(117) 23.0(123) Sodium hexameta phosphate (25%) 6.9 22.0(117) 23.0(123) Sodium hexameta phosphate (50%) 6.9 22.0(117) 23.0(123) Sodium acid pyro phosphate (10%) 4.2 20.0(107) 23.0(123) Tripotassium phos phate (so0A) 11.5 reacted No foam with MAP+ formed Mono aluminum phosphate ** Mono magnesium phosphate From these data, it will be seen that the dispersing agent should be essentially nonreactive and that it should not be used to the extent that it raises the pH of component B above that which prevents the release of carbon dioxide from the calcium carbonate blowing agent. Example 12 A series of resin compositions were made up to form cellular resins using the same components A and B as in Example 5, except that the amount and type of water-repellant surfactant added to component A were varied. The effect of these variations on cell structure of the resulting resins is noted in the following Table 2. Table 2 Effect of Surfactant on Cell Structure wt.% Surfactant Surfactant Cell Struct./Sz,inch (mm) Hydrophobic fumed silica (10%) 0.43 Medium to fine/40.020(0.51) Hydrophobic fumed silica (10%) 1.0 Ultrafine/O.010(0.25) Titanate * 0.43 Large/ < (0.060(1.52) Titanate * 1.0 Medium to Lge./ < 0.040(1.02) Silicone 1.0 Medium/ < (0.030(0.76) Aluminum Stearate 1.0 Medium/0.O30(O.76) Calcium Stearate 1.0 Medium/ < (0.030(0.76) Calcium Stearate 1.5 Medium/ < (0.030(0.76) Zinc Stearate 1.0 Medium/c*0.030(0.76) ' Titanate KR-55 - An allyl di-tridecyl titanium phosphate It will be seen from these data that it is possible to predetermine and control cell size by the selection of the type and amount of surfactant used. Example 13 This example illustrates the effect which the addition of a water-control agent has upon the strength and the moisture content of the resin formed. A first resin was made up in the manner described above using the following: Component A Mono magnesium phosphate 100 parts Silica 100 Wollastonite 10 Component B Sodium hexametaphosphate (50) 40 Magnesium oxide 50 Silicone 1 A second resin was made up on the manner described above using the following: Component A Mono aluminum phosphate 100 parts Alumina trihydrate 100 Wollastonite 10 Component B Trisodium phosphate (5%) 24 Magnesium oxide 70 Silicone 1 The strengths of the resulting resins were measured and weight losses measured when they were heated to 200 C. Finally, they were heated until maximum weight loss was experienced. These results are tabulated in Table 3. Table 3 Strength and Weight losses of Resins Resin Item First Second Strength--modulus of rupture, psi(kg/cm2) 1420 (99.4) 675 (47.3) Weight loss, 5Ó total weight at 2000C 10 12 maximum 12 27 Temperature of maximum loss, OC 350 700 It will be seen from these data that the alumina trihydrate present in the second formulation altered the amount of water retained in the cured resin and the temperature profile for the water removal from the resin. Example 14 Component A Mono aluminum phosphate 100 parts Silica 100 Component B 5% Trisodium phosphate solution 35 Wollastonite (5:1 aspect tatio) 70 The resin had a modulus of rupture of 225 psi (15.8 kg/cm2) after four days and a specific gravity of 1.10. The inorganic resins formed in accordance with this invention have many uses in their noncellular and cellular forms. Because of their noflammability and nonsmoking they may be formed into such structural configurations as panels, walls, doors, piping, and ductwork and used in applications where the burning of such structures is not desirable or cannot be tolerated. These resins may be used as acoustical, electrical or thermal insulation. They may be used to form a pouredin-place foam, to repair cracks, to coat surfaces, and to serve as an adhesive. Unlike many organic resins, the inorganic resins of this invention are resistant to chemicals, organic and inorganic, and they are unaffected by ultraviolet radiation making them particularly suitable for outdoor use in a variety of climates. Finally, the resins of this invention are inexpensive relative to those formed of organic constituents.

Claims: CLAIMS: 1. A two-component system for mixing to form an inorganic resin, which comprises: (a) a liquid component A comprising an aqueous solution of one or both of mono aluminum phosphate and mono magnesium phosphate, the solution having a viscosity of from 700 to 10,000 centipoises; and (b) a liquid component B comprising an aqueous vehicle, a phosphate-reactive constituent which is one or both of wollastonite and magnesium oxide, and a non-reactive dispersing agent, component B having a viscosity permitting it to be rapidly and thoroughly mixed with component A so as to form a slurry which reacts exothermically to form an inorganic resin. 2. A two-component system according to claim 1, in which component A includes an inert, low water-demand filler in an amount up to 50% by weight of the total weight of components A and B. 3. A two-component system according to claim 2, in which the inert filler is silica. 4. A two-component system according to claim 2, in which at least a portion of the filler is a preformed cellular material. 5. A two-component system according to claim 2, in which at least a portion of the filler is a finely divided, chemically hydrated water releasing agent. 6. A two-component system according to any of claims 1 to 5, in which component A also includes wollastonite which is substantially unreactive with mono al,tminum phosphate or mono magnesium phosphate over the time required to formulate component A and to mix it with component B, the quantity of unreactive wollastonite being up to 10% by weight of the total weight of components A and 13. 7. A two-component system according to claim 6, in which the substantially unreactive wollastonite is further characterised as being a finely divided acicular material having an aspect ratio of at least 15:1 and a 2 surface area of less than 1.0 m /gm. 8. A two-component system according to any of claims 1 to 7, in which one or both of component A and component B includes a water-repellent surfactant in a total amount of from 0.2% to 5 by weight of the total weight of components A and B. 9. A two-component system according to claim 8, in which the water-repellent surfactant is a hydrophobic fumed silica1 a titanate, a silicone, a wax, or a stearate. 10. A two-component system according to any of claims 1 to 9, in which the aqueous solution of component A has a solids content of from 20 to 70 weight percent. 11. A two-component system according to any of claims 1 to 10, in which the amount of the aqueous solution of component A is from 20% to 70% by weight of the total weight of components A and B. 12. A two-component system according to any of claims 1 to 11, in which the reactive wollastonite of component B is a finely divided acicular wollastonite having an aspect ratio of less than 10:1 and a surface area of at least 1.0 mê/gm and is present in component B in an amount of up to 4096 by weight of the total weight of components A and 15. 13. A two-component system according to any of claims 1 to 12, in which the non-reactive dispersing agent of component B is a polyphosphate in aqueous solution. 14. A two-component system according to any of claims 1 to 13 and suitable for forming a cellular resin, in which one or both of component A and component B includes a water-repellent surfactant, in which component B includes a blowing agent capable of releasing a gas by reaction, decomposition or vaporization in the slurry, and in which the dispersing agent is one which does not raise the pH of the slurry above 10. 15. A two-component system according to claim 14, in which the blowing agent is calcium carbonate in an amount of from 0.2% to 15% by weight of the total weight of components A and B. 16. A two-component system according to any of claims 1 to 15, in which the weight ratio of the aqueous solution of component A to the phosphate reactive constituent of component B is from 50/50 to 65/35. 17. A two-component system according to any of claims 1 to 16, in which the weight ratio of the mono aluminum phosphate-reactive constituent of component B is from 20/80 to 70/30. 18. A process for forming an inorganic resin which comprises mixing components A and B of the twocomponent system according to any of claims 1 to 17 to form a slurry in which the components react exothermically to set up as an inorganic resin. 19. A process according to claim 18, in which the slurry mixture is directed to a support surface capable of supporting the mixture until the reaction is completed. 20. A process according to claim 19, in which the support surface is a fiberglass mat and the mixture impregnates at least an upper surface of the mat to form a fiber-reinforced article. 21. A process according to claim 19, in which the support surface is a fiberboard and the resin adheres to the fiberboard to form a composite article.

Inventors: PRIOR, WILLIAM L., SARGEANT, WILLIAM C.
Applicants: USG INTERIORS, INC.
Application year: 1983
Main classification: C04B12
IPC codes: C04B28, C04B38