CEMENT FORMULATION

Abstract: This invention relates to a formulation for preparing a dry formulation for preparing an autoclave cured cementitious product comprising: a cementitious material; a siliceous material; and a dehydroxylated clay mineral.

Description: TITLE. CEMENT FORMULATION FIELD OF THE INVENTION This invention relates to a formulation for preparing an autoclave cured cementitious material, to a method of preparing a cementitious product using the formulation and to a shaped article capable of being prepared therefrom. BACKGROUND OF THE INVENTION Autoclave cured cementitious materials are commonly used both with and without reinforcement fibres to manufacture many building products. Un-reinforced autoclave aerated concrete (AAC) building blocks and cellulose fibre reinforced concrete (FRC) flat or profiled sheets and FRC pipes are examples of such products. The raw materials used for the manufacture of autoclave cured cementitious products are typically reinforcing fibre (if required), ground sand, cement and/or lime, water and minor additives. However, it has been difficult to date to obtain impressed autoclave cured cementitious products that are as impermeable to water as post-pressed equivalents. Post-pressing occurs after formation of the product. OBJECT OF THE INVENTION It would be desirable to obtain an autoclave cementitious product that has low water permeability. DISCLOSURE OF THE INVENTION According to a first aspect ofthe invention there is provided a dry formulation for preparing an autoclave cured cementitious product comprising: a cementitious material; a siliceous material; and a dehydroxylated clay mineral. According to a second aspect ofthe invention there is provided an aqueous formulation for preparing an autoclave cured cementitious product comprising: a cementitious material; a siliceous material, a dehydroxylated clay mineral; and water. Throughout this specification, unless indicated otherwise where there is reference to wt%, all values are with respect to the formulation on a dry materials weight basis prior to addition of water and processing. The siliceous material is preferably present in an amount of from 10-80wt%, more preferably 30-70wt%, most preferably 40-65wt%. Preferably the siliceous material is ground sand (also known as silica) or fine quartz. Preferably the siliceous material has an average particle size of 1-50 microns, more preferably 20-30 microns. The cementitious material is preferably present in an amount of from 10-80wt%, more preferably 30-70wt%, most preferably 35-50wt%. Preferably the cementitious material is cement and/or lime and/or lime containing material and includes Portland cement, hydrated lime, lime or mixtures thereof. Preferably the cementitious material has an average particle size of 1-50 microns, more preferably 20-30 microns. The dehydroxylated clay mineral can be dehydroxylated kaolin (also known as metakaolin), dehydroxylated bentonite, dehydroxylated montmorillonite, dehydroxylated illite, dehydroxylated muscovite or dehydroxylated phlogopite etc. Preferably the dehydroxylated clay mineral is metakaolin. Metakaolin (Al 2 O 3 .2SiO 2 ) is a reactive aluminium silicate pozzolan formed by thermal activation (dehydroxylation) of kaolin in the temperature range 450-800°C. The dehydroxylated clay mineral is preferably present in an amount of from 0.25-30wt%, more preferably l-25wt%, most preferably 2- 12wt%. Preferably the dehydroxylated clay mineral has an average particle size of 1-50 microns, more preferably 4-8 microns. The dehydroxylated clay mineral may be in a pure or impure form and includes, impure natural clays containing dehydroxylated clay minerals together with other components. Suitable natural clays include tropical soils, and laterite soils. Also suitable are processed natural clays such as black colliery spoil and slate waste. The formulations can include a fibrous material capable of producing a fibre reinforced product. Suitable fibrous materials include cellulose such as softwood and hardwood cellulose fibres, non wood cellulose fibres, asbestos, mineral wool, steel fibre, synthetic polymers such as polyamides, polyesters, polypropylene, polyacrylonitrile, polyacrylamide, viscose, nylon, PVC, PVA, rayon, glass, ceramic or carbon. Cellulose fibres produced by the Kraft process are preferred. Preferably the fibrous materials are present in a concentration of 0-25 wt%, more preferably 2-16wt%, most preferably 5- 12wt%. When cellulose fibres are used, they are preferably refined to a degree of freeness of between 0 and 800 Canadian Standard Freeness (CSF), more preferably 200- 500 CSF. The formulations can contain 0-40wt% of other additives such as fillers such as mineral oxides, hydroxides and clays, metal oxides and hydroxides, fire retardants such as magnesite, thickeners, silica fume or amorphous silica, colorants, pigments, water sealing agents, water reducing agents, setting rate modifiers, hardeners, filtering aids, plasticisers, dispersants, foaming agents or flocculating agents, water-proofing agents, density modifiers or other processing aids. According to a third aspect ofthe invention there is provided a method for forming an autoclave cured cementitious product comprising: adding a cementitious material, a siliceous material, a dehydroxylated clay mineral and optionally other additives to water to form a slurry; forming a green shaped article by dewatering the slurry; optionally pressing the article; and curing the article in an autoclave. Green shaped articles may be formed from the water borne slurry by any of a number of conventional processes such as the Hatschek sheet process, the Mazza pipe process, the Magnani sheet process, injection moulding, extrusion, hand lay-up, moulding, casting, filter pressing, flow on machine, roll forming, etc., with or without post-formation pressing. After forming, the green article is preferably precured for a short time, preferably 0 to 30 hours then cured by autoclaving preferably in a steam pressurised vessel preferably at 120 to 200°C for 3 to 30 hours, most preferably less than 24 hours. The length of time and temperature chosen for curing is dependant on the formulation, the manufacturing process and the form ofthe article. According to a fourth aspect ofthe invention there is provided a cementitious product comprising the autoclave cured reaction product of a dehydroxylated clay mineral, a cementitious material, a siliceous material and optionally other additives. According to a fifth aspect ofthe invention there is provided a cementitious product comprising the autoclave cured reaction product of a fibrous material, a dehydroxylated clay mineral, a cementitious material, a siliceous material and optionally other additives. Preparing autoclave cured products by adding a dehydroxylated clay mineral to the formulation can improve the strength and toughness ofthe product and reduce water permeability and hygroscopic moisture movement. PREFERRED EMBODIMENT OF THE INVENTION The invention will now be described by way of preferred embodiments with reference to the following examples. Throughout Examples 2 to 6 and 8 water permeability is determined by gluing a 1.2m tall tube to the surface of a test specimen, filling water into the tube to a predetermined height and determining its time rate of fall compared to a control. Carbonated moisture movements are determined after the articles (i.e. filter pads) have been subjected to carbon dioxide gas. Flexural toughness is the total energy per unit volume absorbed by test specimens up to the point of maximum load. EXAMPLE 1 Use of metakaolin in a non-reinforced cement/silica matrix. A bench scale experiment was performed. Standard un-reinforced cement/silica test cubes, bars and disks based on off-white cement, were prepared according to a conventional procedure (formulation 1) without post-pressing and used as a control. Two formulations in accordance with the invention were also prepared without post- pressing (formulations 2 and 3). In formulations 2 and 3 metakaolin was incoφorated into the matrix as a replacement for some ofthe silica. Compositions and amounts of each formulation are shown in Table la. The cement was an off-white cement of greater reactivity than ordinary grey general purpose cement. Specimens were all autoclave cured for eight hours at 180°C. Table la Formulation Off-white Cement Silica Metakaolin 1 40.0wt% 60.0wt% 0.0wt% 2 40.0wt% 58.5wt% 1.5wt% 3 40.0wt% 57.0wt% 3.0wt% Table lb Formulation 1 2 3 Level of metakaolin addition, wt% 0 1.5 3.0 Cube compressive strength, MPa 110 99 91 Bar un-carbonated moisture movement, % 0.25 0.21 0.21 Disk drying mass loss, % per hour 6.2 5.3 4.8 The average measured physical properties and drying rates are shown in Table lb. Drying rate was determined by saturating disks under water until they reached constant mass, drying them in a forced draft oven at 55°C for one hour and determining the mass (of water) lost by drying. It can be seen from Table lb that matrices formulated according to the invention (formulations 2 and 3) exhibit lower drying rates, i.e. high resistance to water permeation. Further the un-carbonated moisture movements ofthe inventive formulations are reduced. All ofthe observed compressive strengths are well above the 85MPa considered reasonable for actual product performance. EXAMPLE 2 Use of metakaolin in cellulose fibre-reinforced concrete filter pads. A bench scale experiment was conducted. Filter pads of cellulose fibre- reinforced concrete with a 40:60 (weight basis) cemen silica ratio were prepared without post-pressing according to a conventional procedure. Formulation 4 was used as a control. Two formulations in accordance with the invention were then prepared with metakaolin incorporated into the matrix (formulations 5 and 6). The composition and amounts of each formulation are shown in Table 2a. Specimens were all autoclave cured for eight hours at 180°C. Table 2a Formulation Cellulose Cement Silica Metakaolin Fire Retardant 4 8.0wt% 35.2wt% 52.8wt% 0wt% 4.0wt% 5 8.0wt% 36.8wt% 53.2wt% 2.0wt% 0wt% 6 8.0wt% 36.8wt% 51.2wt% 4.0wt% 0wt% Table 2b Formulation 4 5 6 Cellulose freeness, CSF 450 450 450 Level of metakaolin addition, wt% 0 2.0 4.0 Saturated flexural strength, MPa 11.8 11.9 12.6 Saturated Young's modulus, GPa 2.9 2.6 3.4 Saturated flexural toughness, KJ/m3 11.0 11. 5 11.4 Uncarbonated moisture movement % 0.17 0.19 0.19 Carbonated moisture movement, % 0.43 0.45 0.47 Water permeation rate, ml/hr 1.00 0.50 0.38 Oven dry density, kg/m3 1270 1270 1270 The resulting average measured physical properties and water permeability rates (using a im high water column) are shown in Table 2b. Filter pads formulated according to the invention (formulations 5 and 6) exhibit improved water permeation resistance without adverse effects on other physical properties. EXAMPLE 3 Effect of cellulose freeness on water permeability reduction effect. A bench scale experiment was conducted. Formulations were used containing cellulose having two different pulp freeness levels to make filter pads without post- pressing via a conventional procedure. Formulations 7 and 9 were used as a control. Formulations 8 and 10 were made in accordance with the present invention and contained 2wt% of metakaolin. Compositions and amounts of each formulation are shown in Table 3a. Specimens were all autoclave cured for eight hours at 180°C. Table 3 a Formulation Cellulose Cement Silica Metakaolin Fire Retardant 7 8.0wt% 35.2wt% 52.8wt% 0wt% 4.0wt% 8 8.0wt% 36.8wt% 53.2wt% 2.0wt% 0wt% 9 8.0wt% 35.2wt% 52.8wt% 0wt% 4.0wt% 10 8.0wt% 36.8wt% 53.2wt% 2.0wt% 0wt% Table 3b Formulation 7 8 9 10 Cellulose freeness, CSF 450 450 141 141 Level of metakaolin addition, wt% 0 2.0 0 2.0 Saturated flexural strength, MPa 11.8 11.9 10.5 11.3 Saturated Young's modulus, GPa 2.9 2.6 3.5 4.3 Saturated flexural toughness, KJ/m3 11.0 11.5 5.1 4.9 Uncarbonated moisture movement % 0.17 0.19 0.18 0.22 Carbonated moisture movement, % 0.43 0.45 0.42 0.36 Water permeation rate, ml hr 1.00 0.50 0.71 0.47 Oven dry density, kg/m3 1270 1270 1270 1250 The physical properties and water permeation rates are shown in Table 3b. Comparison ofthe results for formulations 7, 8, 9 and 10 show that filter pads formulated according to the invention (formulations 8 and 10) exhibit improved water permeation resistance for both pulp freeness levels investigated. EXAMPLE 4 Effect of method of metakaolin addition on permeability. A bench scale experiment was conducted. Filter pads were prepared without post-pressing according to a conventional procedure. Formulations 11 and 13 were used as controls. Formulations 12 and 14 in accordance with the invention contained metakaolin at a level of 2.0wt% using two different addition methods, namely (i) by addition to the matrix mix (formulation 12) and (ii) by addition to the cellulose fibre prior to batching of solids (formulation 14) so that the fibres were effectively pre-coated with the metakaolin. Compositions and amount for each formulation are shown in Table 4a. Specimens were all autoclave cured for eight hours at 180°C. Table 4a Formulation Cellulose Cement Silica Metakaolin Fire Retardant 11 8.0wt% 35.2wt% 52.8wt% 0wt% 4.0wt% 12 8.0wt% 36.8wt% 53.2wt% 2.0wt% 0wt% 13 8.0wt% 35.2wt% 52.8wt% 0wt% 4.0wt% 14 8.0wt% 36.8wt% 53.2wt% 2.0wt% 0wt% Table 4b Formulation 11 12 13 14 Cellulose freeness, CSF 450 450 390 390 Level of metakaolin addition, wt% - 2 - 2 Method of metakaolin addition - Mix addition - Fibre coated Saturated flexural strength, MPa 11.8 11.9 11.1 12.5 Saturated Young's modulus, GPa 2.9 2.6 3.6 3.9 Saturated flexural toughness, KJ/m3 11.0 11.5 6.3 6.6 Uncarbonated moisture movement % 0.17 0.19 0.15 0.19 Carbonated moisture movement, % 0.43 0.45 0.43 0.43 Water permeation rate, ml/hr 1.00 0.50 1.00 0.43 Oven dry density, kg/m3 1270 1270 1330 1270 The physical properties and permeability rates are given in Table 4b, which shows filter pads formulated according to the invention (formulations 12 and 14) exhibit improved water permeation resistance for both methods of metakaolin addition. EXAMPLE 5 Effect of metakaolin addition on toughness and moisture movements A bench experiment was conducted. Filter pads were prepared without post- pressing using a conventional procedure. Formulation 15 was used as a control. Formulations 16 and 17 were prepared in accordance with the invention by incoφorating metakaolin into the matrix by replacement of silica whilst maintaining the amount of cement. The silica ement weight ratio for the control was 50:50. Compositions and amounts of each ofthe formulations are shown in Table 5 a. Specimens were all autoclave cured for eight hours at 180°C. Table 5 a Formulation Cellulose Cement Silica Metakaolin 15 8.0wt% 46.0wt% 46.0wt% 0wt% 16 8.0wt% 46.0wt% 44.0wt% 2.0wt% 17 8.0wt% 46.0wt% 36.0wt% 10.0wt% Table 5b Formulation 15 16 17 Cellulose freeness, CSF 465 357 465 Level of metakaolin addition, wt% 0% 2.0% 10.0% Saturated flexural strength, MPa 14.6 13.8 12.2 Saturated Young's modulus, GPa 3.4 3.5 3.1 Saturated flexural toughness, KJ/m3 8.8 7.8 11.7 Uncarbonated moisture movement % 0.20 0.20 0.18 Carbonated moisture movement, % 0.52 0.49 0.46 Water permeation rate, ml/hr 0.51 0.41 0.23 Oven dry density, kg/m3 1300 1320 1290 The physical properties and resistance to permeation values are shown in Table 5b. Comparison ofthe results of formulations 15, 16 and 17 show that filter pads formulated according to the invention (formulations 16 and 17) exhibit improved water permeation resistance. At a 10wt% level of metakaolin addition (formulation 17) the saturated flexural toughness is significantly improved and post- and pre-carbonation moisture movement is reduced. EXAMPLE 6 Effect of metakaolin and lime additions on toughness and moisture movement. A bench experiment was conducted. Filter pads were prepared via a conventional procedure without post-pressing. Formulation 18 was used as a control. Formulations 19 and 20 were prepared in accordance with the present invention with metakaolin and hydrated lime in the relative weight proportions of 1 :2 were incoφorated into the matrix. In both the control and inventive formulations, a cement:silica ratio of 50:50 was maintained. Compositions and amounts for each formulation are given in Table 6a. Specimens were all autoclave cured for eight hours at 180°C. Table 6a Formulation Cellulose Cement Silica Metakaolin Lime 18 8.0wt% 46.0wt% 46.0wt% 0wt% 0wt% 19 8.0wt% 38.5wt% 38.5wt% 5.0wt% 10.0wt% 20 8.0wt% 34.8wt% 34.8wt% 7.5wt% 15.0wt% Table 6b Formulation 18 19 20 Cellulose freeness, CSF 266 266 266 Level of metakaolin addition, wt% 0 5.0 7.5 Saturated flexural strength, MPa 13.5 11.6 9.6 Saturated Young's modulus, GPa 4.25 3.0 2.5 Saturated flexural toughness, KJ/m3 5.2 9.6 9.2 Uncarbonated moisture movement % 0.21 0.18 0.15 Carbonated moisture movement, % 0.45 0.42 0.40 Water permeation rate, ml/hr 0.21 0.21 0.30 Oven dry density, kg/cm3 1310 1270 1240 The physical properties and resistance to permeation values are shown in Table 6b. It is evident from the table that filter pads formulated according to the invention (formulations 19 and 20) exhibit reduced post- and pre-carbonation moisture movement. Further the flexural toughness is also improved. This is associated with a visible decrease in the oven dry density and a less than expected decrease in flexural strength and Young's modulus. EXAMPLE 7 Effect of metakaolin addition on low density composites A bench scale experiment was conducted. Filter pads all incoφorating a density lowering, autoclave stable modifier additive were prepared via a conventional procedure without post-pressing. Formulations 21 and 23 were used as a control. Formulations 22 and 24 were prepared in accordance with the invention with metakaolin incoφorated into the matrix by replacement of silica and cement while maintaining the cement: silica ratio. Compositions and amounts of each ofthe formulations is shown in Table 7a. Specimens were all autoclave cured for eight hours at 180°C. Table 7a Formulation Cellulose Cement Silica Metakaolin Additive 21 11.3wt% 31.5wt% 47.3wt% 0wt% 10.0wt% 22 11.3wt% 30. 4wt% 45.7wt% 2.7wt% 10.0wt% 23 11.3wt% 27.5wt% 41.3wt% 0wt% 20.0wt% 24 11.3wt% 25.3wt% 38.0wt% 5.4wt% 20.0wt% Table 7b Formulation 21 22 23 24 Cellulose freeness, CSF 380 380 380 380 Level of metakaolin addition, wt% 0 2.7 0 5.4 Saturated flexural strength, MPa 6.7 6.1 4.8 5.7 Saturated flexural toughness, KJ/m3 10.5 12.6 9.6 10.2 Uncarbonated moisture movement % 0.25 0.19 0.26 0.23 Carbonated moisture movement, % 0.40 0.44 0.45 0.64 Carbonation shrinkage, % 0.20 0.15 0.14 0.12 Permeability factor 241 138 138 47 Density, kg/m3 884 1016 913 923 The physical properties and permeability factor values are shown in Table 7b. The permeability factor is a proportionate measure ofthe rate at which water under pressure may be forced through a specimen in a permeability testing cell. Lower values indicate lower water permeability. It is evident from the table that filter pads formulated according to the invention (formulations 22 and 24) exhibit reduced un-carbonated moisture movement, reduced carbonation shrinkage values and reduced permeability to water . Further with metakaolin addition, the flexural toughness is improved (formulation 22) and the flexural strength is increased (formulation 24). EXAMPLE 8 Use of Metakaolin as replacement to cement in cellulose fibre-reinforced cementitious composites A full scale experiment was conducted. Cellulose fibre-reinforced cementitious sheets (6 mm thick) were made using the Hatschek process. Formulation 25 was used as control. Two formulations in accordance with the invention were then prepared with metakaolin incoφorated in the matrix by partial replacement of cement (Formulations 26 and 27). The composition and amounts of each formulation are shown in Table 8a. All sheets were autoclave cured for eight hours at 180°C. Table 8a Formulation Cellulose Cement Silica Metakaolin Pigment Fire Retardant 25 8.0 wt% 35 wt% 60 wt% 0.0 wt% 4.0 wt% 4.0 wt% 26 7.0 wt% 29 wt% 54 wt% 6.0 wt% 4.0 wt% 0.0 wt% 27 7.0 wt% 25 wt% 58 wt% 6.0 wt% 4.0 wt% 0.0 wt% Table 8b Formulation 25 26 27 Cellulose Freeness, CSF 450 450 450 Level of metakaolin addition, wt% 0.0 6.0 6.0 Saturated flexural strength, MPa 12.47 12.30 12.40 Saturated flexural toughness, KJ/m3 12.50 10.50 9.50 Uncarbonated moisture movement, % 0.17 0.15 0.15 Water Permeation Rate, ml/hr 1.13 0.67 0.54 Saturated Young's modulus, GPa 4.54 5.07 5.15 Oven dry density, kg/m3 1400 1440 1400 Comparison ofthe results for formulations 25, 26 and 27 is shown in Table 8b. It can be seen that cellulose fibre-reinforced sheets formulated according to the invention with metakaolin incoφorated as cement replacement (formulations 26 and 27), exhibited comparable saturated flexural strengths and significantly less water permeation rates compared to sheets made with Formulation 25. It is further observed that uncarbonated moisture movements were reduced. The results achieved in this example show that, at the above indicated addition level, metakaolin contributes to the strength of cement deficient composites in addition to reducing their permeability rate and moisture movement. The values for water permeability reduction evidenced by the un-pressed products using formulations in accordance with the invention as evidenced by the examples are values which would normally only be obtained by an additional step of post-pressing products with the attendant increase in density. It is believed that post- pressing will further enhance the observed reduction in water permeability. Further from the examples it can be seen that metakaolin addition results in reduced un-carbonated and post-carbonation moisture movements of autoclave composites and in some cases to reduced carbonation shrinkage. Flexural toughness (the energy required to fracture a flexural test specimen) ofthe autoclave composites is also improved when metakaolin is present as an additive in the matrix forming material. The formulations ofthe present invention are suitable for the production of autoclave cured cementitious products for both internal and external applications. Although the invention has been described with reference only to selected examples, it will be appreciated by those skilled in the art that the invention may be embodied in many other forms.

Claims: CLAIMS 1. A dry formulation for preparing an autoclave cured cementitious product comprising: a cementitious material; a siliceous material; and a dehydroxylated clay mineral. 2. A formulation according to claim 1 wherein the siliceous material is present in an amount of from 10 to 80 wt. % based on the total weight ofthe dry formulation. 3. A formulation according to claim 1 or 2 wherein the siliceous material is ground sand or fine quartz. 4. A formulation according to any one of claims 1 to 3 wherein the siliceous material has an average particle size of 1 to 50 microns. 5. A formulation according to any one of claims 1 to 4 wherein the cementitious material is present in an amount of from 10 to 80 wt. % based on the total weight ofthe dry formulation. 6. A formulation according to any one of claims 1 to 5 wherein the cementitious material is cement and/or lime and/or lime containing material. 7. A formulation according to any one of claims 1 to 6 wherein the cementitious material has an average particle size of from 1 to 50 microns. 8. A formulation according to any one of claims 1 to 7 wherein the dehydroxylated clay mineral is dehydroxylated kaolin, dehydroxylated bentonite, dehydroxylated montmorrilonite, dehydroxylated muscovite or dehydroxylated phlogopite. 9. A formulation according to claim 8 wherein the dehydroxylated clay mineral is dehydroxylated kaolin. 10. A formulation according to any one of claims 1 to 9 wherein the dehydroxylated clay mineral is present in an amount from 0.25 to 30 wt. % based on the total weight of the dry formulation. 11. A formulation according to any one of claims 1 to 10 wherein the dehydroxylated clay mineral has an average particle size of 1 to 50 microns. 12. A formulation according to any one of claims 1 to 11 further comprising a fibrous material. 13. A formulation according to claim 12 wherein the fibrous material is selected from cellulose, asbestos, mineral wool, steel fibre, synthetic polymers, glass, ceramic or carbon. 14. A formulation according to claim 13 wherein the fibrous material is cellulose having a degree of freeness of between 0 and 800 CSF. 15. A formulation according to any one of claims 12 to 14 wherein the fibrous material is present in an amount up to 25 wt. % based on the total weight ofthe dry formulation. 16. A formulation according to any one of claims 1 to 15 further comprising at least one other additive selected from mineral oxides, mineral hydroxides, mineral clays, metal oxides, metal hydroxides, fire retardants, thickeners, silica fume, amoφhous silica, colorants, pigments, water sealing agents, water reducing agents, setting rate modifiers, hardeners, filtering aids, plasticizers, dispersants, foaming agents, flocculating agents, water-proofing agents, density modifiers or other processing aids. 17. An aqueous formulation for preparing an autoclave cured cementitious product comprising: a cementitious material; a siliceous material; a dehydroxylated clay mineral; water; and optionally other additives. 18. A method for forming an autoclave cured cementitious product comprising: adding a cementitious material, a siliceous material, a dehydroxylated clay mineral and optionally other additives to water to form a slurry; forming a green shaped article by dewatering the slurry; optionally pressing the article; and curing the article in an autoclave. 19. A method according to claim 18, further comprising a fibrous material. 20. A method according to claim 18 or 19 wherein the green shaped articles are formed from the slurry with or without post-formation pressing, by means of one or more ofthe processes selected from the Hatshek sheet process, the Mazza pipe process, the Magnani sheet process, injection moulding, extrusion, hand lay-up, moulding, casting, filter pressing, flow on machine or roll forming. 21. A method according to any one of claims 18 to 20 wherein the green article is precured prior to curing. 22. A method according to any one of claims 18 to 21 wherein the article is cured by autoclaving in a steam pressurised vessel at 120 to 200°C for 3 to 30 hours. 23. A cementitious product comprising the autoclave cured reaction product of a dehydroxylated clay mineral, a cementitious material, a siliceous material and optionally other additives. 24. A cementitious product comprising the autoclave cured reaction product of a fibrous material, a dehydroxylated clay mineral, a cementitious material, a siliceous material and optionally other additives.

Inventors: DUSELIS STEVEN ALFRED, GLEESON JAMES ALBERT, KLIMESCH DANIELLE SIMONE, NAJI BASIL TAHA, SLOANE BRIAN PATRICK, STITT DAVID MALCOLM, DUSELIS, STEVEN, ALFRED, GLEESON, JAMES, ALBERT, KLIMESCH, DANIELLE, SIMONE, NAJI, BASIL, TAHA, SLOANE, BRIAN, PATRICK, STITT, DAVID, MALCOLM
Applicants: JAMES HARDIE RES PTY LTD, JAMES HARDIE RESEARCH PTY. LIMITED
Application year: 1996
Main classification: C04B14
IPC codes: B28B1, C04B14, C04B28