WO2002008139A2 - Method of increasing the heat insulating capacity of a material - Google Patents

Method of increasing the heat insulating capacity of a material Download PDF

Info

Publication number
WO2002008139A2
WO2002008139A2 PCT/IB2001/001253 IB0101253W WO0208139A2 WO 2002008139 A2 WO2002008139 A2 WO 2002008139A2 IB 0101253 W IB0101253 W IB 0101253W WO 0208139 A2 WO0208139 A2 WO 0208139A2
Authority
WO
WIPO (PCT)
Prior art keywords
hydrate
sulphate
hydrogel
water
product
Prior art date
Application number
PCT/IB2001/001253
Other languages
French (fr)
Other versions
WO2002008139A3 (en
Inventor
Michael Windsor Symons
Original Assignee
Balmoral Technologies (Pty) Limited
Windsor Technologies Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Balmoral Technologies (Pty) Limited, Windsor Technologies Limited filed Critical Balmoral Technologies (Pty) Limited
Priority to AU2001269366A priority Critical patent/AU2001269366A1/en
Publication of WO2002008139A2 publication Critical patent/WO2002008139A2/en
Publication of WO2002008139A3 publication Critical patent/WO2002008139A3/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/009After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B22/00Use of inorganic materials as active ingredients for mortars, concrete or artificial stone, e.g. accelerators, shrinkage compensating agents
    • C04B22/0066Compounds chosen for their high crystalwater content
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B26/00Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
    • C04B26/02Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/45Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
    • C04B41/50Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials
    • C04B41/5007Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials with salts or salty compositions, e.g. for salt glazing
    • C04B41/5014Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials with salts or salty compositions, e.g. for salt glazing containing sulfur in the anion, e.g. sulfides
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/60After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only artificial stone
    • C04B41/61Coating or impregnation
    • C04B41/65Coating or impregnation with inorganic materials
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00Fireproofing materials
    • C09K21/02Inorganic materials
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16LPIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L59/00Thermal insulation in general
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/20Resistance against chemical, physical or biological attack
    • C04B2111/28Fire resistance, i.e. materials resistant to accidental fires or high temperatures

Definitions

  • This invention relates to a method of increasing the heat insulating capacity of a material, such as a finished product made from exfoliated vermiculite particles or expanded perlite particles.
  • the finished product may be for example a panel or a board or the like.
  • a building panel For a building panel to be able to withstand the temperatures associated with a fully developed fire, i.e up to 1000°C, several attributes are required. These include dimensional stability, refractoriness, the absence of cracking and cohesive strength. However, above all, the thermal insulation properties of the building panel are important. By this is meant the resistance of the building panel to the transference of the heat of the fire through the body of the building panel, and the speed with which this occurs in fire.
  • a method of increasing the heat insulating capacity of a material including the step of including in the material a product which releases water at elevated temperatures selected from the group consisting of (i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and (iii) a combination of two or more hydrates and/or hydrogels; the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder.
  • the product i.e the hydrate or the hydrogel may be included in the material by impregnation as an aqueous solution, and subsequent drying.
  • the method may include the steps of:
  • step (b) drying the impregnated material to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel.
  • the material is preferably provided in a substantially dry condition.
  • step (b) the impregnated material is preferably dried to its equilibrium moisture content for the climate or environment in which it is to be used.
  • the material to be so impregnated and dried may be a formed product such as a panel, board, door or the like, or may be a starting material for such a formed product.
  • the material for use in step (a) is a cohesive product, the cohesive product being formed from a starting material by the steps of:
  • feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an amount of expanded aluminium silicate, all in the form of substantially dry finely divided particles;
  • thermosetting resin in finely divided dry powder form or in liquid form
  • step (3) subjecting the starting material of step (2) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product.
  • the material for use in step (a) is a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element.
  • the product, i.e the hydrate or the hydrogel may be included in the material by including in the material a precursor of the hydrate or the hydrogel, in dry form, and subsequently providing to the material water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
  • the method may include the steps of:
  • step (C) forming the product of step (B) into a cohesive product
  • the starting material for use in step (A) is formed by the steps of:
  • feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an expanded aluminium silicate, all in the form of substantially dry finely divided particles;
  • thermosetting resin in finely divided dry powder form or in liquid form
  • steps (C) and (D) comprise:
  • step (C) subjecting the product of step (B) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product; and (D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel, and for hydration of any hydraulic binder present to cause the hydraulic binder to set.
  • step (C) the precursor must not decompose to give off gaseous products during step (C) which would result in failure of the product of step (B).
  • a building component including a product which releases water at elevated temperatures selected from the group consisting of: (i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and
  • the crux of the invention is a method of increasing the heat insulating capacity of a material by including in the material a product which is either a water soluble crystallised compound in. the form of a hydrate with two or more molecules of water, or an inorganic hydrogel, or a combination of two or more hydrates and/or hydrogels, the hydrate or hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder.
  • the hydrate or the hydrogel may be included in the material by impregnation as an aqueous solution, and subsequent drying.
  • the impregnation and drying may be carried out by:
  • the material may be any material suitable for impregnation, in particular building elements such as panels, boards, doors and the like. Alternatively, the material may be a starting material for such a product.
  • the preferred material is a cohesive product formed from exfoliated vermiculite or expanded perlite, a thermosetting resin, and optionally a hydraulic binder.
  • Another preferred material is a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element.
  • the first component used in forming the starting material is a feedstock comprising expanded perlite or exfoliated vermiculite or a mixture of the two, optionally also including an expanded aluminium silicate, in substantially dry finely divided particle form.
  • the particles preferably have a diameter of 0,5 mm or less. The preferred particle size ranges from 2 micron to 500 micron diameter inclusive.
  • a suitable vermiculite is RSU submicron, with a particle size of less than 250 micron, by Phalaborwa Mining Company.
  • Other examples are Zonolite No 4 and No 5 by W R Grace.
  • Genulite M105 having a bulk density of 105 g/l
  • M75 having a bulk density of 75 g/l
  • An example of a suitable expanded aluminium silicate is one with a bulk density in the range of from 150 to 220 g/l and a pH of from 6 to 7,5, such as ASP 170 by Engelhard.
  • the second component used in forming the starting material is a thermosetting resin in finely divided dry powder form or in liquid form.
  • thermosetting resin By “finely divided” there is meant that the thermosetting resin must have a particle size of 98% passing a 200 mesh screen or finer (i.e a 74 micron screen or finer.)
  • the thermosetting resin is preferably a novolac phenol formaldehyde resin with a suitable catalyst in finely divided dry powder form.
  • Other thermosetting resins which may be used include isocyanate thermosetting resins, also known as polyurethane resins, together with their precursors such as MDIs, unsaturated polyester resins, phenol formaldehyde resole resins, epoxy resins, methacrylic acid ester resins, acrylic resins, urea formaldehyde resins, melamine formaldehyde resins and similar resins.
  • thermosetting resin is preferably used in an amount of from 2% to 20% inclusive of the thermosetting resin by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
  • the third optional component for use in forming the starting material is a hydraulic binder in finely divided dry powder form.
  • a hydraulic binder is a substance which hydrates and sets in combination with water.
  • hydraulic binder must have a particle size of 98% passing a 200 mesh screen or finer (i.e a 74 micron screen or finer).
  • Portland cement typically has a Blaine of 475, i.e 475m 2 per kg.
  • the hydraulic binder is preferably chosen from the group comprising Portland cement, high alumina cement, gypsum cement, calcium sulphate hemihydrate either in the alpha or beta form, magnesium oxychloride, magnesium oxysulphate, a calcium sulphoaluminate cement, and pozzolans such ground granulated blast furnace slag, or a combination of any two or more thereof.
  • the hydraulic binder is preferably used in an amount of from 5% to 40% inclusive of the hydraulic binder, by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
  • hydraulic binder in themselves hydrate when exposed to water.
  • the hydraulic binder is used as a binder and in addition to the hydrate and not as a substitute therefor.
  • the starting material is subjected to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form a cohesive product.
  • the starting material may be subjected to a temperature of from 125°C to 255°C inclusive and a pressure of from 10 to 70 kg/cm 2 inclusive.
  • step (a)) of the method of the invention the cohesive product is impregnated with an aqueous solution of a water soluble compound which compound either when crystallised forms a hydrate with two or more molecules of water, or forms a hydrogel, the hydrate or hydrogel decomposing at a decomposition temperature of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, the water being provided in an amount sufficient for the hydration of any hydraulic binder present to cause the hydraulic binder to set.
  • step (b)) of the method of the invention the product of the previous step is dried to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel.
  • Suitable water soluble compounds which form hydrates with two or more molecules of water include the following:
  • Metal sulphate hydrates such as for example aluminium sulphate hydrate (AI 2 (SO 4 ) 3 .18H 2 O); cadmium sulphate hydrate (3CdSO 4 .8H 2 O or CdSO 4 .4H 2 O); chromic sulphate hydrate (Cr 2 (SO 4 ) 3 .15H 2 O or Cr 2 (SO ) 3 .18H 2 O) which loses 12H 2 O at 100°C; sodium sulphate decahydrate, also known as Glauber's salt (Na 2 SO .10H 2 O); magnesium sulphate (MgSO 4 .7H 2 O) which is a crystalline heptahydrate also known as Epsom salts, a solution of which has a pH of 6,8 and which loses 6H 2 O at 150°C and 7H 2 O at 200°C; and zinc sulphate hydrate (ZnSO 4 .7H 2 O) which loses 5H 2 O at 70°C eventually forming
  • Disodium tetraborate decahydrate (Na 2 B 4 O 7 .10H 2 O), also known as borax, which is soluble in water and which loses 8H 2 O at 75°C and a further 10H 2 O at 320°C.
  • This hydrate has a solids % of about 53% and a crystalline water % of about 47%.
  • M stands for a metal cation (including ammonium)
  • M + and M 3+ are different.
  • the metal cation M + is preferably selected from the group consisting of aluminium, iron, chromium, manganese and cobalt, and the metal cation M + is preferably selected from the group consisting of potassium, sodium, ammonium and cerium.
  • Suitable double salts include: aluminium potassium sulphate also known as potassium alum
  • AIK(SO 4 ) 2 .12H 2 O or AI 2 (SO 4 ) 3 .K 2 SO 4 .24H 2 O which loses 18H 2 O at 64,5°C; aluminium sodium sulphate also known as soda alum (AINa(SO 4 ) 2 .12H 2 O or
  • AI 2 (SO 4 ) 3 .Na 2 SO 4 .24H 2 O); chromium potassium sulphate also known as chrome alum (CrK(SO 4 ) 2 .12H 2 O); aluminium ammonium sulphate also known as ammonium alum
  • chrome ammonium alum 120°C; chromium ammonium sulphate also known as chrome ammonium alum
  • Sodium carbonate decahydrate also known as sal soda (Na 2 .CO 3 .10H 2 O);
  • Sodium metasilicate which has the generic formula Na 2 SiO 3 .9H 2 O, and which loses 6H 2 O at 100°C.
  • An example is Silchem 3379 by Silicate and Chemical Industries of South Africa, which as a typical solution has an SG of 1 ,395, a composition of 29,07% SiO 2 and 8,81% Na 2 0, a solid percentage of 37,88 in water, and a weight ratio of SiO 2 to Na 2 0 of 3,3:1.
  • Sodium metacilicate also has the advantage of being refractory and thereby contributing to the cohesive strength of the finished product.
  • Potassium silicate This compound has a typical SG of 1 ,33, a composition of 23,86% SiO 2 and 11 ,11% K 2 O, a solid percentage of 35 in water, and a weight ratio of SiO 2 to K 2 O of 2.1 :1 to 2.5:1. Potassium silicate has the advantage of being highly refractory and imposes an acid resistance to the final product.
  • Ferroso-ferric chloride Ferroso-ferric chloride (FeCI 2 .2FeCI 3 .18H 2 O);
  • Dibasic sodium phosphate Na 2 HPO .12H 2 O which loses 12H 2 O at 180°C;
  • Potassium pyrophosphate (K 4 P 2 O 7 .3H 2 O) which loses 2H 2 O at 180°C and 3H 2 O at 300°.
  • Magnesium orthophosphate (Mg 3 (PO 4 ) 2 .22H 2 O) which loses 18H 2 O at 100°C.
  • Alumina trihydrate (AI 2 O 3 .3H 2 O).
  • the impregnating composition may include two or more suitable hydrates, for example, to give water release over a range of temperatures.
  • suitable hydrates for example, to give water release over a range of temperatures.
  • Another example of a suitable combination is magnesium sulphate and sodium borate which release water over a temperature range of from 75°C up to 330°C.
  • a suitable hydrogel is a silica gel formed from a desiccated sodium silicate, the silica gel being hygroscopic and rapidly forming a saturated, stable, inorganic hydrogel on contact with water.
  • the water soluble compound or the compound which forms the hydrogel or the combination thereof is preferably dissolved in water in an amount of from 2% to 50% inclusive on a mass basis, depending upon the solubility of the compound in water.
  • the aqueous solution of the water soluble compound or the compound which forms the hydrogel may be impregnated into the cohesive product in any suitable manner.
  • the cohesive product may be placed in a pressure cylinder and optionally subjected to a pressure of from 10 to 15 kPa for 15 minutes. Thereafter the cylinder is flooded with the impregnating solution, and a pressure of from 200 to 600 kPa is applied for 10 minutes until penetration is complete.
  • the impregnated cohesive product may then be removed from the pressure cylinder. Thereafter, the impregnated cohesive product is dried in a suitable kiln. Drying is preferably humidity drying with air flows in the region of 5 m/s to 8 m/s at temperatures preferably not exceeding 70°C.
  • the material which has been impregnated must be dried at a temperature below that at which the hydrate decomposes to release the water of hydration or crystallisation or at which the hydrogel decomposes to release water, or at which the hydrate or hydrogel itself starts to decompose.
  • the material for use in step (a) may be a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element.
  • the foam element may be made of any suitable thermoplastic or thermosetting foam, including polyurethane, phenolic foams, silicone, polyimide and polyvinyl chloride.
  • the preferred foam is a polyurethane foam.
  • Polyurethane foams are generally formed from an isocyanate such as for example methyl phenyl di-isocyanate (MDI) or toluene di-isocynate (TDI)
  • isocyanate such as for example methyl phenyl di-isocyanate (MDI) or toluene di-isocynate (TDI)
  • the polyurethane foams can be formed by reacting the isocyanates with hydroxyl compounds containing two or more reactive sites.
  • the foam must be a rigid or semi-rigid foam and must be open celled.
  • the size of the open cells is determined during the manufacture of the foam and is desirably in the range of from 1mm to 10mm inclusive in diameter, more preferably from 1mm to 3mm inclusive in diameter.
  • a typical example of the manufacture of a polyurethane foam is the reaction of an MDI with a polyol in the presence of some water. The reaction between these compounds releases carbon dioxide which blows to form the foam.
  • the foam element may be any suitable foam element such as for example a length of foam for a wall insulating panel, or a foam tile for roof insulation or any other element utilised for insulation.
  • a foam element is preferably impregnated with an aqueous solution of an alkali metal silicate or a compound which forms a silica gel. After drying, a coating of the alkali metal silicate or the silica gel is left on a part or all of the surfaces of the cells of the foam element.
  • the alkali metal silicate may be a sodium silicate having a formula varying from Na 2 O.3.75SiO 2 to 2Na 2 O.SiO 2 and with various proportions of water.
  • sodium silicate is also intended to include sodium metasilicate e.g sodium metasilicate pentahydrate, sodium sesquisilicate and sodium orthosilicate.
  • silicate An example of a preferred sodium silicate is Silchem 3379 by Silicate and Industries as described above. This silicate is characterised by its propensity to intumesce or froth when subjected to fire.
  • the alkali metal silicate may also be a potassium silicate in which the weight ratio of SiO 2 to K 2 O varies from 2.1 :1 to 2.5:1.
  • silica gel is generally formed in situ in the foam element by reaction between an alkali metal silicate as described above, and an acid or an acidic gas.
  • the acid used is preferably a weak acid such as boric acid (H 3 BO 3 ) which reacts with sodium silicate to form a silica gel.
  • a weak acid such as boric acid (H 3 BO 3 ) which reacts with sodium silicate to form a silica gel.
  • an acidic gas such as carbon dioxide may be used to react with the alkali metal silicate to form the silica gel.
  • the coating may also include a crystalline hydrate which decomposes at a temperature of from 40°C to 500°C inclusive to release water from the hydrate.
  • the solution of the alkali metal silicate which is impregnated into the foam element may contain a water soluble crystalline hydrate dissolved therein. On drying of the impregnated foam element, the water is removed, leaving behind the crystalline hydrate.
  • a suitable water soluble crystalline hydrate is magnesium sulphate, MgSO 4 .7H 2 O as described above.
  • an insoluble crystalline hydrate may be dispersed, as very fine particles, in the solution of the alkali metal silicate.
  • An example of a suitable insoluble crystalline hydrate is aluminium trihydrate, AI 2 O 3 .3H 2 O.
  • the method of impregnating the foam element will now be described.
  • the first step of the method is to impregnate the foam element with an aqueous solution of the alkali metal silicate.
  • This solution may optionally contain a water soluble crystalline hydrate dissolved therein or a water insoluble crystalline hydrate dispersed therein.
  • the solids percentage in the aqueous solution is determined by the viscosity required of the solution, which in turn is dependent on the size of the open cells of the foam element.
  • the impregnation may be achieved for example by cascading the aqueous solution onto the foam element and allowing it to run through the foam element, thereby lining part or all of the surfaces of the open cells of the foam element with an alkali metal silicate film, the thickness of which is dependent on the viscosity of the solution.
  • the foam element may be subjected to a vacuum in a cylinder, whereafter the cylinder is flooded with the aqueous solution.
  • the second step of the method of the invention is to remove any excess of the aqueous solution from the foam element. This may be achieved for example by allowing the excess aqueous solution to drain from the foam element, optionally assisted by a vacuum.
  • the third step of the method of the invention is to impregnate the foam element with an acid or an acidic gas which reacts with the alkali metal silicate to form a silica gel.
  • the impregnation of the foam element with the acid or the acidic gas may be carried out before or after the impregnation of the foam element with the alkali metal silicate.
  • the foam element is first impregnated with the acid or the acidic gas and then with the alkali metal silicate.
  • a suitable acid is a weak acid such as boric acid.
  • the boric acid reacts with the alkali metal silicate to form a silica gel which coats the surfaces of the open cells of the foam element.
  • the fourth step of the method of the invention is to remove any excess of the acid from the foam element.
  • the foam element may simply be impregnated with an alkali metal silicate solution (without the use of an acid or acidic gas).
  • the fifth step of the method of the invention is to dry the product of the fourth step to give the insulating product.
  • the drying is preferably carried out with the application of heat, preferably not exceeding an initial temperature of 80°C, and dropping to 40°C as the excess water is driven off.
  • the result is an insulating product where the surfaces of the open cells of the foam element are coated with a coating of the alkali metal silicate or the silica gel, both of which have a cooling effect in fire by the release of water.
  • the coating tends to intumesce or froth at elevated temperatures, adding to the insulation and preventing a flame path in fire.
  • an open cell polyurethane foam treated with a sodium silicate solution containing a crystalline hydrate, and preferably acidified to form a silica gel using either a weak acid such as boric acid or using an acidic gas such as carbon dioxide can resist a fully developed fire for 90 minutes at a thickness of 50 mm with the temperature of an unexposed surface remaining below 110°C.
  • a weak acid such as boric acid
  • an acidic gas such as carbon dioxide
  • the foam element may have a thin outer skin or skins placed thereon, either before or after coating with the alkali metal silicate or the silica gel.
  • a polyurethane foam may be foamed between two thin outer skins to give a foam element which is then treated as described above.
  • the foam element may be produced and then have adhesively applied to one or more surfaces thereof a thin outer skin.
  • the thin outer skins may be made of any suitable materials such as for example:
  • Sheet metal skins e.g steel or aluminium having a thickness of from 0.2 mm to
  • Dry pressed mineral skins having a thickness of from 1.5 mm to 12 mm, preferably from 1.5 mm to 6 mm inclusive, and with a density exceeding
  • Pure vermiculite sheets having a thickness of from 1.5 mm to 6 mm inclusive and a density in the range of from 1300 kg/m 3 to 1700 kg/m 3 , formed from exfoliated vermiculite bound with a suitable resin such as for example a polyurethane resin or a phenol formaldehyde novolac resin;
  • thermosetting resin such as a phenol formaldehyde resole resin or a polyurethane resin
  • the product i.e the hydrate or the hydrogel may be included in the material by including in the material a precursor of a hydrate or a hydrogel, in dry form, and subsequently providing to the material water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
  • the method may include the steps of:
  • step (C) forming the product of step (B) into a cohesive product
  • the starting material comprises exfoliated vermiculite or expanded perlite, a thermosetting resin, and optionally a hydraulic binder.
  • a precursor which is either an anhydrous or partially hydrous precursor of a compound which, when contacted with water, forms a hydrate with two or more molecules of water, or which is a precursor of a compound which, when contacted with water, forms a hydrogel, the hydrate or the hydrogel decomposing at a decomposition temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, the precursor not decomposing to give off gaseous products during formation of the cohesive product which would result in failure of the cohesive product, with the proviso that the precursor is not a hydraulic binder.
  • Suitable precursor compounds for the hydrate include the following: Metal sulphates such as for example aluminium sulphate (AI 2 (SO 4 ) 3 ) which hydrates to AI 2 (SO 4 ) 3 .18H 2 O; cadmium sulphate (CdSO 4 ) which hydrates to 3CdSO 4 .8H 2 O or CdSO 4 .4H 2 O; chromic sulphate (Cr 2 (SO 4 ) 3 ) which hydrates to Cr 2 (SO 4 ) 3 .15H 2 O or Cr 2 (SO 4 ) 3 .18H 2 O; sodium sulphate (Na 2 SO 4 ) which hydrates to sodium sulphate decahydrate, also known as Glauber's salt, i.e Na 2 SO 4 .
  • Metal sulphates such as for example aluminium sulphate (AI 2 (SO 4 ) 3 ) which hydrates to AI 2 (SO 4 ) 3 .18H 2 O
  • CdSO 4
  • M stands for a metal cation (including ammonium) and M + and M 3 3 + + are different.
  • the metal cation M 3+ is preferably selected form the group consisting of aluminium, iron, chromium, manganese and cobalt, and the metal cation M + is preferably selected from the group consisting of potassium, sodium, ammonium and cerium.
  • AIK(SO 4 ) 2 .12H 2 O or AI 2 (SO 4 ) 3 .K 2 SO 4 .24H 2 O which loses 18H 2 O at 64,5°C; aluminium sodium sulphate also known as soda alum (AINa(SO 4 ) 2 .12H 2 O or
  • AI 2 (SO 4 ) 3 .Na 2 SO 4 .24H 2 O); chromium potassium sulphate also known as chrome alum (CrK(SO 4 ) 2 .12H 2 O); aluminium ammonium sulphate also known as ammonium alum
  • chrome ammonium alum 120°C; chromium ammonium sulphate also known as chrome ammonium alum
  • Potassium silicate anhydrous, which hydrates to potassium silicate.
  • Ferroso-ferric chloride anhydrous, i.e FeCI 2 .2FeCI 3 , which hydrates to
  • AI 2 O 3 reactive gamma alumina, i.e AI 2 O 3 which hydrates to AI 2 O 3 .3H 2 O.
  • a suitable precursor for a hydrogel is sodium silicate in dry powder form, e.g SP 33 by Silicate and Chemical Industries of South Africa, having a solids percentage of 84% and a weight ratio SiO 2 to Na 2 O of 3,3:1.
  • the anhydrous or partially hydrous precursor must not decompose to give off gaseous products during formation of the cohesive product. In other words, the precursor must not decompose nor give rise to any free water molecules which would cause an increase in pressure in the product being pressed, resulting in its destruction when the pressure is released.
  • the anhydrous or partially hydrous precursor is preferably used in an amount of from 2% to 40% inclusive of the precursor by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
  • step (C) of the method the starting material is subjected to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form a cohesive product. Suitable conditions are set out above.
  • step (D) of the method there is provided to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel, and for hydration of any hydraulic binder present to cause the hydraulic binder to set.
  • the water may be impregnated into the cohesive product by immersion of the cohesive product in water in a suitable chamber.
  • a preferred method of hydration is the use of low pressure steam or air saturated with water vapour, at temperatures in the range of from 40°C to 100°C inclusive, under pressure in a pressure cylinder, until the cohesive product has been subjected to sufficient water vapour to ensure the hydration of the precursor, and of any hydraulic binder present.
  • step (D) If necessary, any water in excess of that required in step (D) is removed, i.e the finished product is dried to the equilibrium moisture content.
  • a panel for the production of a fire rated door core was produced having a composition of 33% calcium sulphate hemi hydrate, 8% novolac phenol formaldehyde resin, and 59% expanded perlite of a particle size less than 0.5 mm diameter.
  • the panel was pressed at a temperature of about 200°C to product a composite having a density of about 500 kg/m 3 at a thickness of 40 mm.
  • This dry composite was then impregnated with an aqueous solution containing 50% aluminium sulphate and 50% sodium sulphate, the sulphates being dissolved in the water in an amount of 15% by mass (combined sulphates).
  • the impregnated composite was then dried to a free water percentage of about 4%, i.e the water contained in the solution of the water soluble compound was substantially removed.
  • the water of crystallisation or hydration formed when the aluminium sulphate and sodium sulphate crystallised was however retained within the impregnated composite.
  • the impregnated composite when subjected to a fully developed fire with a furnace temperature exceeding 1000°C in a positive pressure furnace withstood the fire for 120 minutes, after which the side of the impregnated panel remote from the fire had a temperature not exceeding 110°C. Further, the integrity and degree of warpage in the composite panel remained substantially unchanged.
  • a composition was formed as follows:
  • Resin - Novolac 602 by Schenectady Corporation 8% The composition was pressed to a density of about 450 kg/m 3 to give a cohesive product.
  • the cohesive product was impregnated with water and then dried at 45°C at 15% relative humidity in a drier with an air speed of 6 m/s until the product reached a constant weight, to give the final product.
  • Tests were conducted on finished products made by the method of the invention compared to finished products not including a hydrate or a hydrogel.
  • the products were as follows:
  • Comparative products comprising 28% gypsum, 8% resin and 64% vermiculite particles, were prepared by pressing at a defined temperature and pressure. The products were then impregnated with water only and dried.
  • Products of the invention comprising 28% gypsum, 8% resin and either 64% vermiculite particles (indicated by a V) or 64% perlite particles (indicated by a
  • a feedstock was prepared from:
  • the feedstock was pressed to a cohesive board having a density of about 500 kg/m 3 at 200°C.
  • the cohesive board was post impregnated with a 12,5% solution by mass of magnesium sulphate in water.
  • the resulting impregnated product was dried at 40°C by humidity drying to a free water percentage of ,5% and a total percentage of water of crystallisation of 8,75%.
  • a length of an open cell polyurethane foam with a cell size in the range of 1 mm to 3 mm inclusive was immersed in a 10% solution of boric acid in water. The excess solution was drained from the length of foam and the length of foam was partially dried.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Structural Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Thermal Insulation (AREA)
  • Building Environments (AREA)

Abstract

A method of increasing the heat insulating capacity of a material such as a building component is achieved by including in the material a product which releases water at elevated temperatures. The product may be a water soluble crystallised compound in the form of a hydrate with two or more molecules of water, an inorganic hydrogel, or a combination of two or more hydrates or hydrogels, the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel to slow the progress of temperature elevation through the material.

Description

METHOD OF INCREASING THE HEAT INSULATING CAPACITY
OF A MATERIAL
BACKGROUND OF THE INVENTION
This invention relates to a method of increasing the heat insulating capacity of a material, such as a finished product made from exfoliated vermiculite particles or expanded perlite particles. The finished product may be for example a panel or a board or the like.
For a building panel to be able to withstand the temperatures associated with a fully developed fire, i.e up to 1000°C, several attributes are required. These include dimensional stability, refractoriness, the absence of cracking and cohesive strength. However, above all, the thermal insulation properties of the building panel are important. By this is meant the resistance of the building panel to the transference of the heat of the fire through the body of the building panel, and the speed with which this occurs in fire.
TION COW While various methods and means are known to increase the fire resistance of materials, there is always a need for new methods of this kind.
SUMMARY OF THE INVENTION
According to a first aspect of the invention there is provided a method of increasing the heat insulating capacity of a material, including the step of including in the material a product which releases water at elevated temperatures selected from the group consisting of (i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and (iii) a combination of two or more hydrates and/or hydrogels; the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder.
In one aspect of the invention, the product, i.e the hydrate or the hydrogel may be included in the material by impregnation as an aqueous solution, and subsequent drying.
For example, the method may include the steps of:
(a) impregnating the material with an aqueous solution of:
(a1) a water soluble compound which when crystallised forms the hydrate; or (a2) a compound which forms the hydrogel; or (a3) a combination of (a1) and (a2); and
(b) drying the impregnated material to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel. In step (a) the material is preferably provided in a substantially dry condition.
In step (b) the impregnated material is preferably dried to its equilibrium moisture content for the climate or environment in which it is to be used.
The material to be so impregnated and dried may be a formed product such as a panel, board, door or the like, or may be a starting material for such a formed product.
In a preferred method of this aspect of the invention, the material for use in step (a) is a cohesive product, the cohesive product being formed from a starting material by the steps of:
(1) providing a feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an amount of expanded aluminium silicate, all in the form of substantially dry finely divided particles;
(2) mixing the feedstock with
(2.1) a suitable amount of a thermosetting resin in finely divided dry powder form or in liquid form; and
(2.2) optionally a suitable amount of a hydraulic binder in finely divided dry powder form; to give the starting material; and
(3) subjecting the starting material of step (2) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product.
In another preferred method of this aspect of the invention the material for use in step (a) is a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element. In another aspect of the invention, the product, i.e the hydrate or the hydrogel may be included in the material by including in the material a precursor of the hydrate or the hydrogel, in dry form, and subsequently providing to the material water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
For example, the method may include the steps of:
(A) providing a starting material;
(B) mixing the starting material with a suitable amount of the precursor;
(C) forming the product of step (B) into a cohesive product; and
(D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
In a preferred method of this aspect of the invention, the starting material for use in step (A) is formed by the steps of:
(1) providing a feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an expanded aluminium silicate, all in the form of substantially dry finely divided particles;
(2) mixing the feedstock with:
(2.1) a suitable amount of a thermosetting resin in finely divided dry powder form or in liquid form; and
(2.2) optionally a suitable amount of a hydraulic binder in finely divided dry powder form; to give the starting material.
In this case steps (C) and (D) comprise:
(C) subjecting the product of step (B) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product; and (D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel, and for hydration of any hydraulic binder present to cause the hydraulic binder to set.
It is to be noted that the precursor must not decompose to give off gaseous products during step (C) which would result in failure of the product of step (B).
According to a second aspect of the invention there is provided a building component including a product which releases water at elevated temperatures selected from the group consisting of: (i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and
(iii) a combination of two or more hydrates and/or hydrogels; the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder.
DESCRIPTION OF EMBODIMENTS
The crux of the invention is a method of increasing the heat insulating capacity of a material by including in the material a product which is either a water soluble crystallised compound in. the form of a hydrate with two or more molecules of water, or an inorganic hydrogel, or a combination of two or more hydrates and/or hydrogels, the hydrate or hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder. When a material treated by the method of the invention is subjected to a fire, as the material heats up above 40°C, depending upon the nature of the hydrate or the hydrogel in the material, water is released at a temperature or temperatures up to 500°C, either by being endothermically split from the hydrate or evaporated from the hydrogel, thereby removing the latent heat of vaporisation from the mateπal and cooling it, until all the water is removed. This has the effect of slowing the progress of temperature elevation through the material.
In one aspect of the invention, the hydrate or the hydrogel may be included in the material by impregnation as an aqueous solution, and subsequent drying.
For example, the impregnation and drying may be carried out by:
(a) impregnating the material with an aqueous solution of:
(a1) a water soluble compound which when crystallised forms the hydrate; or (a2) a compound which forms the hydrogel; or (a3) a combination of (a1) and (a2); and
(b) drying the impregnated material to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel.
The material may be any material suitable for impregnation, in particular building elements such as panels, boards, doors and the like. Alternatively, the material may be a starting material for such a product. The preferred material is a cohesive product formed from exfoliated vermiculite or expanded perlite, a thermosetting resin, and optionally a hydraulic binder. Another preferred material is a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element. Thus, in a preferred method of this aspect of the invention, there is provided a method of preparing a finished product from a cohesive product, the cohesive product being formed from a starting material including exfoliated vermiculite, expanded perlite, or a mixture thereof, a thermosetting resin and optionally a hydraulic binder.
Thus the first component used in forming the starting material is a feedstock comprising expanded perlite or exfoliated vermiculite or a mixture of the two, optionally also including an expanded aluminium silicate, in substantially dry finely divided particle form. In this regard, the particles preferably have a diameter of 0,5 mm or less. The preferred particle size ranges from 2 micron to 500 micron diameter inclusive.
An example of a suitable vermiculite is RSU submicron, with a particle size of less than 250 micron, by Phalaborwa Mining Company. Other examples are Zonolite No 4 and No 5 by W R Grace.
An example of a suitable perlite is Genulite M105 (having a bulk density of 105 g/l) or M75 (having a bulk density of 75 g/l) by Chemserve Perlite.
An example of a suitable expanded aluminium silicate is one with a bulk density in the range of from 150 to 220 g/l and a pH of from 6 to 7,5, such as ASP 170 by Engelhard.
The second component used in forming the starting material is a thermosetting resin in finely divided dry powder form or in liquid form.
By "finely divided" there is meant that the thermosetting resin must have a particle size of 98% passing a 200 mesh screen or finer (i.e a 74 micron screen or finer.) The thermosetting resin is preferably a novolac phenol formaldehyde resin with a suitable catalyst in finely divided dry powder form. Other thermosetting resins which may be used include isocyanate thermosetting resins, also known as polyurethane resins, together with their precursors such as MDIs, unsaturated polyester resins, phenol formaldehyde resole resins, epoxy resins, methacrylic acid ester resins, acrylic resins, urea formaldehyde resins, melamine formaldehyde resins and similar resins.
The thermosetting resin is preferably used in an amount of from 2% to 20% inclusive of the thermosetting resin by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
The third optional component for use in forming the starting material is a hydraulic binder in finely divided dry powder form. A hydraulic binder is a substance which hydrates and sets in combination with water.
By "finely divided" there is meant that the hydraulic binder must have a particle size of 98% passing a 200 mesh screen or finer (i.e a 74 micron screen or finer). For example, Portland cement typically has a Blaine of 475, i.e 475m2 per kg.
The hydraulic binder is preferably chosen from the group comprising Portland cement, high alumina cement, gypsum cement, calcium sulphate hemihydrate either in the alpha or beta form, magnesium oxychloride, magnesium oxysulphate, a calcium sulphoaluminate cement, and pozzolans such ground granulated blast furnace slag, or a combination of any two or more thereof.
The hydraulic binder is preferably used in an amount of from 5% to 40% inclusive of the hydraulic binder, by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
It is to be noted that certain hydraulic binders in themselves hydrate when exposed to water. In the method of the present invention, the hydraulic binder is used as a binder and in addition to the hydrate and not as a substitute therefor.
Other optional components may be included in the starting material, such as an amount of reinforcing fibres.
In the third step of the method of the invention, the starting material is subjected to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form a cohesive product.
For example, the starting material may be subjected to a temperature of from 125°C to 255°C inclusive and a pressure of from 10 to 70 kg/cm2 inclusive.
In the next step (step (a)) of the method of the invention, the cohesive product is impregnated with an aqueous solution of a water soluble compound which compound either when crystallised forms a hydrate with two or more molecules of water, or forms a hydrogel, the hydrate or hydrogel decomposing at a decomposition temperature of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, the water being provided in an amount sufficient for the hydration of any hydraulic binder present to cause the hydraulic binder to set.
In the next step (step (b)) of the method of the invention, the product of the previous step is dried to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel. Suitable water soluble compounds which form hydrates with two or more molecules of water include the following:
Metal sulphate hydrates such as for example aluminium sulphate hydrate (AI2(SO4)3.18H2O); cadmium sulphate hydrate (3CdSO4.8H2O or CdSO4.4H2O); chromic sulphate hydrate (Cr2(SO4)3.15H2O or Cr2(SO )3.18H2O) which loses 12H2O at 100°C; sodium sulphate decahydrate, also known as Glauber's salt (Na2SO .10H2O); magnesium sulphate (MgSO4.7H2O) which is a crystalline heptahydrate also known as Epsom salts, a solution of which has a pH of 6,8 and which loses 6H2O at 150°C and 7H2O at 200°C; and zinc sulphate hydrate (ZnSO4.7H2O) which loses 5H2O at 70°C eventually forming the anhydride at 280°C.
Disodium tetraborate decahydrate (Na2B4O7.10H2O), also known as borax, which is soluble in water and which loses 8H2O at 75°C and a further 10H2O at 320°C. This hydrate has a solids % of about 53% and a crystalline water % of about 47%.
A double salt of the formula
M+M3+(SO4)2.12H2O wherein M stands for a metal cation (including ammonium), and M+ and M3+ are different. The metal cation M + is preferably selected from the group consisting of aluminium, iron, chromium, manganese and cobalt, and the metal cation M+ is preferably selected from the group consisting of potassium, sodium, ammonium and cerium.
Examples of suitable double salts include: aluminium potassium sulphate also known as potassium alum
(AIK(SO4)2.12H2O or AI2(SO4)3.K2SO4.24H2O) which loses 18H2O at 64,5°C; aluminium sodium sulphate also known as soda alum (AINa(SO4)2.12H2O or
AI2(SO4)3.Na2SO4.24H2O); chromium potassium sulphate also known as chrome alum (CrK(SO4)2.12H2O); aluminium ammonium sulphate also known as ammonium alum
(AINH4(SO4)2.12H2O or AI2(SO4)3(NH4)2SO4.24H2O) which loses 20H2O at
120°C; chromium ammonium sulphate also known as chrome ammonium alum
(CrNH4(SO4)2.12H2O); and ferric potassium sulphate also known as iron alum (FeK(SO4)2.12H2O);
Sodium carbonate decahydrate also known as sal soda (Na2.CO3.10H2O);
Sodium metasilicate, which has the generic formula Na2SiO3.9H2O, and which loses 6H2O at 100°C. An example is Silchem 3379 by Silicate and Chemical Industries of South Africa, which as a typical solution has an SG of 1 ,395, a composition of 29,07% SiO2 and 8,81% Na20, a solid percentage of 37,88 in water, and a weight ratio of SiO2 to Na20 of 3,3:1. Sodium metacilicate also has the advantage of being refractory and thereby contributing to the cohesive strength of the finished product.
Potassium silicate. This compound has a typical SG of 1 ,33, a composition of 23,86% SiO2 and 11 ,11% K2O, a solid percentage of 35 in water, and a weight ratio of SiO2 to K2O of 2.1 :1 to 2.5:1. Potassium silicate has the advantage of being highly refractory and imposes an acid resistance to the final product.
Ferroso-ferric chloride (FeCI2.2FeCI3.18H2O);
Dibasic sodium phosphate (Na2HPO .12H2O) which loses 12H2O at 180°C;
Potassium pyrophosphate (K4P2O7.3H2O) which loses 2H2O at 180°C and 3H2O at 300°.
Magnesium orthophosphate (Mg3(PO4)2.22H2O) which loses 18H2O at 100°C. Alumina trihydrate (AI2O3.3H2O).
The impregnating composition may include two or more suitable hydrates, for example, to give water release over a range of temperatures. For example, one may use a combination of potassium silicate both for its refractory properties and for its release of water, in combination with a compatible alum salt.
Another example of a suitable combination is magnesium sulphate and sodium borate which release water over a temperature range of from 75°C up to 330°C.
An example of a suitable hydrogel is a silica gel formed from a desiccated sodium silicate, the silica gel being hygroscopic and rapidly forming a saturated, stable, inorganic hydrogel on contact with water.
The water soluble compound or the compound which forms the hydrogel or the combination thereof is preferably dissolved in water in an amount of from 2% to 50% inclusive on a mass basis, depending upon the solubility of the compound in water.
The aqueous solution of the water soluble compound or the compound which forms the hydrogel may be impregnated into the cohesive product in any suitable manner. For example, the cohesive product may be placed in a pressure cylinder and optionally subjected to a pressure of from 10 to 15 kPa for 15 minutes. Thereafter the cylinder is flooded with the impregnating solution, and a pressure of from 200 to 600 kPa is applied for 10 minutes until penetration is complete. The impregnated cohesive product may then be removed from the pressure cylinder. Thereafter, the impregnated cohesive product is dried in a suitable kiln. Drying is preferably humidity drying with air flows in the region of 5 m/s to 8 m/s at temperatures preferably not exceeding 70°C.
It is to be noted that the material which has been impregnated must be dried at a temperature below that at which the hydrate decomposes to release the water of hydration or crystallisation or at which the hydrogel decomposes to release water, or at which the hydrate or hydrogel itself starts to decompose.
In another preferred method of this aspect of the invention the material for use in step (a) may be a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element.
The foam element may be made of any suitable thermoplastic or thermosetting foam, including polyurethane, phenolic foams, silicone, polyimide and polyvinyl chloride.
The preferred foam is a polyurethane foam.
Polyurethane foams are generally formed from an isocyanate such as for example methyl phenyl di-isocyanate (MDI) or toluene di-isocynate (TDI)
The polyurethane foams can be formed by reacting the isocyanates with hydroxyl compounds containing two or more reactive sites.
As indicated above, the foam must be a rigid or semi-rigid foam and must be open celled.
The size of the open cells is determined during the manufacture of the foam and is desirably in the range of from 1mm to 10mm inclusive in diameter, more preferably from 1mm to 3mm inclusive in diameter. A typical example of the manufacture of a polyurethane foam is the reaction of an MDI with a polyol in the presence of some water. The reaction between these compounds releases carbon dioxide which blows to form the foam.
The foam element may be any suitable foam element such as for example a length of foam for a wall insulating panel, or a foam tile for roof insulation or any other element utilised for insulation.
A foam element is preferably impregnated with an aqueous solution of an alkali metal silicate or a compound which forms a silica gel. After drying, a coating of the alkali metal silicate or the silica gel is left on a part or all of the surfaces of the cells of the foam element.
The alkali metal silicate may be a sodium silicate having a formula varying from Na2O.3.75SiO2 to 2Na2O.SiO2 and with various proportions of water.
The term sodium silicate is also intended to include sodium metasilicate e.g sodium metasilicate pentahydrate, sodium sesquisilicate and sodium orthosilicate.
An example of a preferred sodium silicate is Silchem 3379 by Silicate and Industries as described above. This silicate is characterised by its propensity to intumesce or froth when subjected to fire.
The alkali metal silicate may also be a potassium silicate in which the weight ratio of SiO2 to K2O varies from 2.1 :1 to 2.5:1.
An example of a suitable potassium silicate is Silchem K2166 by Silicate and Chemical Industries which has a percentage of SiO2 of 23.86%, a percentage of K2O of 11.11%, a solids percentage of 34.99% and a weight ratio of SiO2 to K2O of 2.15:1. Alternatively, there may be used a silica gel. The silica gel is generally formed in situ in the foam element by reaction between an alkali metal silicate as described above, and an acid or an acidic gas.
The acid used is preferably a weak acid such as boric acid (H3BO3) which reacts with sodium silicate to form a silica gel.
As an alternative to the use of an acid, an acidic gas such as carbon dioxide may be used to react with the alkali metal silicate to form the silica gel.
The coating may also include a crystalline hydrate which decomposes at a temperature of from 40°C to 500°C inclusive to release water from the hydrate.
In a first alternative, the solution of the alkali metal silicate which is impregnated into the foam element may contain a water soluble crystalline hydrate dissolved therein. On drying of the impregnated foam element, the water is removed, leaving behind the crystalline hydrate. An example of a suitable water soluble crystalline hydrate is magnesium sulphate, MgSO4.7H2O as described above.
In a second alternative, an insoluble crystalline hydrate may be dispersed, as very fine particles, in the solution of the alkali metal silicate. In this case, it is obviously important that the particle size of the crystalline hydrate is small enough to fit inside the cells of the open cell foam element. An example of a suitable insoluble crystalline hydrate is aluminium trihydrate, AI2O3.3H2O.
The use of a crystalline hydrate increases the water holding capacity of the insulating product, which is advantageous in fire.
The method of impregnating the foam element will now be described. The first step of the method is to impregnate the foam element with an aqueous solution of the alkali metal silicate. This solution may optionally contain a water soluble crystalline hydrate dissolved therein or a water insoluble crystalline hydrate dispersed therein.
The solids percentage in the aqueous solution is determined by the viscosity required of the solution, which in turn is dependent on the size of the open cells of the foam element.
The impregnation may be achieved for example by cascading the aqueous solution onto the foam element and allowing it to run through the foam element, thereby lining part or all of the surfaces of the open cells of the foam element with an alkali metal silicate film, the thickness of which is dependent on the viscosity of the solution.
Alternatively the foam element may be subjected to a vacuum in a cylinder, whereafter the cylinder is flooded with the aqueous solution.
The second step of the method of the invention is to remove any excess of the aqueous solution from the foam element. This may be achieved for example by allowing the excess aqueous solution to drain from the foam element, optionally assisted by a vacuum.
When it is desired that the foam element be coated with a silica gel, then the third step of the method of the invention is to impregnate the foam element with an acid or an acidic gas which reacts with the alkali metal silicate to form a silica gel.
The impregnation of the foam element with the acid or the acidic gas may be carried out before or after the impregnation of the foam element with the alkali metal silicate. In a preferred method, the foam element is first impregnated with the acid or the acidic gas and then with the alkali metal silicate.
As indicated above, a suitable acid is a weak acid such as boric acid. The boric acid reacts with the alkali metal silicate to form a silica gel which coats the surfaces of the open cells of the foam element.
The fourth step of the method of the invention is to remove any excess of the acid from the foam element.
Alternatively the foam element may simply be impregnated with an alkali metal silicate solution (without the use of an acid or acidic gas).
The fifth step of the method of the invention is to dry the product of the fourth step to give the insulating product.
The drying is preferably carried out with the application of heat, preferably not exceeding an initial temperature of 80°C, and dropping to 40°C as the excess water is driven off.
The result is an insulating product where the surfaces of the open cells of the foam element are coated with a coating of the alkali metal silicate or the silica gel, both of which have a cooling effect in fire by the release of water. In addition, and in particular with the silica gel, the coating tends to intumesce or froth at elevated temperatures, adding to the insulation and preventing a flame path in fire.
For example, an open cell polyurethane foam treated with a sodium silicate solution containing a crystalline hydrate, and preferably acidified to form a silica gel using either a weak acid such as boric acid or using an acidic gas such as carbon dioxide, can resist a fully developed fire for 90 minutes at a thickness of 50 mm with the temperature of an unexposed surface remaining below 110°C. In addition, such an insulating product, when used as an acoustic ceiling tile, has a good noise reduction co-efficient and is inexpensive.
The foam element may have a thin outer skin or skins placed thereon, either before or after coating with the alkali metal silicate or the silica gel.
For example, a polyurethane foam may be foamed between two thin outer skins to give a foam element which is then treated as described above.
As an alternative, the foam element may be produced and then have adhesively applied to one or more surfaces thereof a thin outer skin.
The thin outer skins may be made of any suitable materials such as for example:
Sheet metal skins, e.g steel or aluminium having a thickness of from 0.2 mm to
2 mm inclusive, which may be flat or surface embossed;
Dry pressed mineral skins having a thickness of from 1.5 mm to 12 mm, preferably from 1.5 mm to 6 mm inclusive, and with a density exceeding
1 100 kg/m3, produced for example from expanded perlite or exfoliated vermiculite bound with an inorganic binder;
Pure vermiculite sheets having a thickness of from 1.5 mm to 6 mm inclusive and a density in the range of from 1300 kg/m3 to 1700 kg/m3, formed from exfoliated vermiculite bound with a suitable resin such as for example a polyurethane resin or a phenol formaldehyde novolac resin;
Paper laminates, the paper being laminated using a suitable thermosetting resin such as a phenol formaldehyde resole resin or a polyurethane resin; and
Glass fibre reinforced polyurethane, polyester or phenol formaldehyde resole resin sheets. In the second aspect of the invention, the product, i.e the hydrate or the hydrogel may be included in the material by including in the material a precursor of a hydrate or a hydrogel, in dry form, and subsequently providing to the material water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
For example, the method may include the steps of:
(A) providing a starting material;
(B) mixing the starting material with a suitable amount of the precursor;
(C) forming the product of step (B) into a cohesive product; and
(D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
In a preferred method of this aspect of the invention, the starting material comprises exfoliated vermiculite or expanded perlite, a thermosetting resin, and optionally a hydraulic binder.
Details of suitable components for the starting material, viz. the exfoliated vermiculite, expanded perlite, thermosetting resin, and hydraulic binder are set out above.
There is included in the starting material a suitable amount of a precursor which is either an anhydrous or partially hydrous precursor of a compound which, when contacted with water, forms a hydrate with two or more molecules of water, or which is a precursor of a compound which, when contacted with water, forms a hydrogel, the hydrate or the hydrogel decomposing at a decomposition temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, the precursor not decomposing to give off gaseous products during formation of the cohesive product which would result in failure of the cohesive product, with the proviso that the precursor is not a hydraulic binder. Suitable precursor compounds for the hydrate include the following: Metal sulphates such as for example aluminium sulphate (AI2(SO4)3) which hydrates to AI2(SO4)3.18H2O; cadmium sulphate (CdSO4) which hydrates to 3CdSO4.8H2O or CdSO4.4H2O; chromic sulphate (Cr2(SO4)3) which hydrates to Cr2(SO4)3.15H2O or Cr2(SO4)3.18H2O; sodium sulphate (Na2SO4) which hydrates to sodium sulphate decahydrate, also known as Glauber's salt, i.e Na2SO4. 0H2O; magnesium sulphate (MgSO4) which hydrates to MgSO4.7H2O; and zinc sulphate (ZnSO4) which hydrates to ZnSO4.7H2O. Sodium borate, anhydrous (Na2B O7) which hydrates to Na2B4O7.10H2O. A double salt of the formula
Λ+H Λ3+ (SO4) wherein M stands for a metal cation (including ammonium) and M+ and M 33++ are different. The metal cation M3+ is preferably selected form the group consisting of aluminium, iron, chromium, manganese and cobalt, and the metal cation M+ is preferably selected from the group consisting of potassium, sodium, ammonium and cerium. These double salts hydrate to give double salts of the formula
M+M3+(SO4)2.12H2O, examples being: aluminium potassium sulphate also known as potassium alum
(AIK(SO4)2.12H2O or AI2(SO4)3.K2SO4.24H2O) which loses 18H2O at 64,5°C; aluminium sodium sulphate also known as soda alum (AINa(SO4)2.12H2O or
AI2(SO4)3.Na2SO4.24H2O); chromium potassium sulphate also known as chrome alum (CrK(SO4)2.12H2O); aluminium ammonium sulphate also known as ammonium alum
(AINH4(SO4)2.12H2O or AI2(SO4)3(NH4)2SO4.24H2O) which loses 20H2O at
120°C; chromium ammonium sulphate also known as chrome ammonium alum
(CrNH4(SO4)2.12H2O); and ferric potassium sulphate also known as iron alum (FeK(SO )2.12H2O); Sodium carbonate, anhydrous, i.e Na2CO3, or sodium carbonate monohydrate, i.e Na2CO3.H2O which hydrate to sodium carbonate decahydrate, also known as sal soda, i.e Na2CO3.10H2O;
Sodium metasilicate, anhydrous, i.e Na2SiO3, which hydrates to sodium metasilicate, i.e Na2SiO3.9H2O which loses 6H2O at 100°C;
Potassium silicate, anhydrous, which hydrates to potassium silicate.
Ferroso-ferric chloride, anhydrous, i.e FeCI2.2FeCI3, which hydrates to
FeCI2.2FeCI3.18H2O;
Dibasic sodium phosphate, anhydrous, i.e Na2HPO4, which hydrates to
Na2HPO4.12H2O;
Potassium pyrophosphate, anhydrous, (K P2O7) which hydrates to potassium pyrophosphate K P2O7.3H2O;
Magnesium orthophosphate, anhydrous (Mg3(PO )2) which hydrates to magnesium orthophosphate Mg3(PO )2.22H2O;
reactive gamma alumina, i.e AI2O3 which hydrates to AI2O3.3H2O.
A suitable precursor for a hydrogel is sodium silicate in dry powder form, e.g SP 33 by Silicate and Chemical Industries of South Africa, having a solids percentage of 84% and a weight ratio SiO2 to Na2O of 3,3:1.
The anhydrous or partially hydrous precursor must not decompose to give off gaseous products during formation of the cohesive product. In other words, the precursor must not decompose nor give rise to any free water molecules which would cause an increase in pressure in the product being pressed, resulting in its destruction when the pressure is released. -99-
The anhydrous or partially hydrous precursor is preferably used in an amount of from 2% to 40% inclusive of the precursor by mass of the total mass of the feedstock, the thermosetting resin and the hydraulic binder, i.e total mass of the cohesive product before hydration.
In step (C) of the method, the starting material is subjected to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form a cohesive product. Suitable conditions are set out above.
In step (D) of the method, there is provided to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel, and for hydration of any hydraulic binder present to cause the hydraulic binder to set.
When reference is made to water, this is intended to include the use of liquid water as well as the use of water vapour or steam.
The water may be impregnated into the cohesive product by immersion of the cohesive product in water in a suitable chamber.
A preferred method of hydration is the use of low pressure steam or air saturated with water vapour, at temperatures in the range of from 40°C to 100°C inclusive, under pressure in a pressure cylinder, until the cohesive product has been subjected to sufficient water vapour to ensure the hydration of the precursor, and of any hydraulic binder present.
If necessary, any water in excess of that required in step (D) is removed, i.e the finished product is dried to the equilibrium moisture content.
Examples of the invention will now be given. Example 1
A panel for the production of a fire rated door core was produced having a composition of 33% calcium sulphate hemi hydrate, 8% novolac phenol formaldehyde resin, and 59% expanded perlite of a particle size less than 0.5 mm diameter. The panel was pressed at a temperature of about 200°C to product a composite having a density of about 500 kg/m3 at a thickness of 40 mm.
This dry composite was then impregnated with an aqueous solution containing 50% aluminium sulphate and 50% sodium sulphate, the sulphates being dissolved in the water in an amount of 15% by mass (combined sulphates). The impregnated composite was then dried to a free water percentage of about 4%, i.e the water contained in the solution of the water soluble compound was substantially removed. The water of crystallisation or hydration formed when the aluminium sulphate and sodium sulphate crystallised was however retained within the impregnated composite.
The impregnated composite, when subjected to a fully developed fire with a furnace temperature exceeding 1000°C in a positive pressure furnace withstood the fire for 120 minutes, after which the side of the impregnated panel remote from the fire had a temperature not exceeding 110°C. Further, the integrity and degree of warpage in the composite panel remained substantially unchanged.
Example 2
A composition was formed as follows:
Exfoliated vermiculite particles 67%
Aluminium sulphate (AI2(SO4)3) 15%
Gypsum 10%
Resin - Novolac 602 by Schenectady Corporation 8% The composition was pressed to a density of about 450 kg/m3 to give a cohesive product. The cohesive product was impregnated with water and then dried at 45°C at 15% relative humidity in a drier with an air speed of 6 m/s until the product reached a constant weight, to give the final product.
Tests were conducted on finished products made by the method of the invention compared to finished products not including a hydrate or a hydrogel. The products were as follows:
COMP 1 AND COMP 2
Comparative products comprising 28% gypsum, 8% resin and 64% vermiculite particles, were prepared by pressing at a defined temperature and pressure. The products were then impregnated with water only and dried.
VAS, PAS. PS, PA, VA. AND VS
Products of the invention comprising 28% gypsum, 8% resin and either 64% vermiculite particles (indicated by a V) or 64% perlite particles (indicated by a
P) were prepared under the same conditions as the comparative products.
The products were then impregnated with water containing 10% of aluminium sodium alum (AS) or sodium sulphate (S) or aluminium sulphate (A) and dried under the same conditions as the comparative products
The products were then analysed and the theoretical percentage gypsum, as if this was the only compound containing crystalline water present in the product, was calculated. The results are set out in Table 1. Table 1
Figure imgf000026_0001
It can be seen that in the products of the invention, the theoretical percentage of gypsum is significantly higher than for the comparative products, indicating an increase in the crystalline water, attributable to the presence of the hydrate compound.
In addition for the product VAS the crystalline water loss commenced at about 93°C whereas for the product COMP 1 the crystalline water loss only commenced at about 125°C.
Example 3
A feedstock was prepared from:
Zonolite No 5 exfoliated vermiculite particles, by W R Grace 69%
Calcium sulphate β-hemi-hydrate 30%
Novalac resin Code 602 by Schenectady 3%
12mm chopped strand fibre glass by Owens Corning 8%
The feedstock was pressed to a cohesive board having a density of about 500 kg/m3 at 200°C.
After cooling, the cohesive board was post impregnated with a 12,5% solution by mass of magnesium sulphate in water. The resulting impregnated product was dried at 40°C by humidity drying to a free water percentage of ,5% and a total percentage of water of crystallisation of 8,75%.
Example 4
A length of an open cell polyurethane foam with a cell size in the range of 1 mm to 3 mm inclusive was immersed in a 10% solution of boric acid in water. The excess solution was drained from the length of foam and the length of foam was partially dried.
Thereafter there was cascaded through the length of foam a 26% solids in water solution of sodium silicate (Code 3379 by Silchem). Excess of the solution was removed immediately. The length of foam was then dried at a temperature of about 60°C with an air speed of 6 m/s to form a rigid insulating product.

Claims

CLAIMS A method of increasing the heat insulating capacity of a material including the step of including in the material a product which releases water at elevated temperatures selected from the group consisting of: (i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and (iii) a combination of two or more hydrates and/or hydrogels; the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder. A method according to claim 1 wherein the product is included in the material by impregnation as an aqueous solution and subsequent drying. A method according to claim 2 including the steps of: (a) impregnating the material with an aqueous solution of:
(a1) a water soluble compound which when crystallised forms the hydrate; or (a2) a compound which forms the hydrogel; or (a3) a combination of (a1) and (a2); and
(b) drying the impregnated material to induce crystallisation of the compound to form the hydrate or gelling of the compound to form the hydrogel, at a temperature below the decomposition temperature of the hydrate or the hydrogel.
A method according to claim 3 wherein the material for use in step (a) is a cohesive product, the cohesive product being formed from a starting material by the steps of: (1) providing a feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an amount of expanded aluminium silicate, all in the form of substantially dry finely divided particles;
(2) mixing the feedstock with:
(2.1) a suitable amount of a thermosetting resin in finely divided dry powder form or in liquid form; and
(2.2) optionally a suitable amount of a hydraulic binder in finely divided dry powder form; to give the starting material; and
(3) subjecting the starting material of step (2) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product.
A method according to claim 2 wherein the material for use in step (a) is a rigid or a semi-rigid open cell thermoplastic or thermosetting foam element.
A method according to claim 1 wherein the product is included in the material by including in the material a precursor of the hydrate or the hydrogel, in dry form, and subsequently providing to the material water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel.
A method according to claim 6 including the steps of:
(A) providing a starting material;
(B) mixing the starting material with a suitable amount of the precursor;
(C) forming the product of step (B) into a cohesive product; and
(D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel. A method according to claim 7 wherein the starting material for use in step (A) is formed by the steps of:
(1) providing a feedstock selected from the group consisting of exfoliated vermiculite and expanded perlite or a mixture thereof, the feedstock optionally including an expanded aluminium silicate, all in the form of substantially dry finely divided particles;
(2) mixing the feedstock with:
(2.1) a suitable amount of a thermosetting resin in finely divided dry powder form or in liquid form; and
(2.2) optionally a suitable amount of a hydraulic binder in finely divided dry powder form; to give the starting material.
A method according to claim 8 wherein steps (C) and (D) comprise:
(C) subjecting the product of step (B) to suitable conditions of temperature and pressure to cause the thermosetting resin to set to form the cohesive product; and
(D) providing to the cohesive product water in an amount sufficient for the hydration of the precursor to form the hydrate or the hydrogel, and for hydration of any hydraulic binder present to cause the hydraulic binder to set.
A method according to any one of claims 1 to 9 wherein the water soluble crystallised compound in the form of a hydrate with two or more molecules of water is selected from the group consisting of metal sulphate hydrates; disodium tetraborate decahydrate; a double salt of the formula M+M3+(SO4)2.12H2O wherein M stand for a metal cation and M+ and M3+ are different; sodium carbonate decahydrate; sodium metasilicate; potassium silicate; ferroso-ferric chloride; dibasic sodium phosphate; potassium pyrophosphate; magnesium orthophosphate; and alumina trihydrate. A method according to claim 10 wherein the metal sulphate hydrate is selected from the group consisting of aluminium sulphate hydrate, cadmium sulphate hydrate, chromic sulphate hydrate, sodium sulphate decahydrate, magnesium sulphate heptahydrate, and zinc sulphate hydrate.
A method according to claim 10 wherein the double salt is selected from the group consisting of aluminium potassium sulphate; aluminium sodium sulphate; chromium potassium sulphate; aluminium ammonium sulphate; chromium ammonium sulphate; and ferric potassium sulphate.
A method according to any one of claims 1 to 9 wherein the inorganic hydrogel is a silica gel formed from sodium silicate.
A method according to any one of claims 6 to 9 wherein the precursor of the hydrate is selected from the group consisting of a metal sulphate; sodium borate, anhydrous; a double salt of the formula M+M3+(SO4)2 wherein M stands for a metal cation and M+ and M3+ are different; sodium carbonate, anhydrous; sodium metasilicate, anhydrous; potassium silicate, anhydrous; ferroso-ferric chloride anhydrous; dibasic sodium phosphate, anhydrous; potassium pyrophosphate, anhydrous; magnesium orthophosphate, anhydrous; and reactive gamma alumina.
A method according to claim 14 wherein the metal sulphate is selected from the group consisting of aluminium sulphate, cadmium sulphate, chromic sulphate, sodium sulphate, magnesium sulphate, and zinc sulphate
A method addording to claim 14 wherein in the double salt of the formula M+M3+ (SO )2, the metal cation M3+ is selected from the group consisting of aluminium, iron, chromium, manganese and cobalt, and the metal Sl-
cation M+ is selected from the group consisting of potassium, sodium, ammonium and cerium.
A method according to any one of claims 6 to 9 wherein the precursor of the hydrogel is sodium silicate in dry powder form.
A building component including a product which releases water at elevated temperatures selected from the group consisting of:
(i) a water soluble crystallised compound in the form of a hydrate with two or more molecules of water; (ii) an inorganic hydrogel; and
(iii) a combination of two or more hydrates and/or hydrogels; the hydrate or the hydrogel decomposing at a temperature in the range of from 40°C to 500°C inclusive to release water from the hydrate or the hydrogel, with the proviso that the hydrate is not a hydrated hydraulic binder.
A building component according to claim 18 wherein the water soluble crystallised compound in the form of the hydrate with two or more molecules of water is selected from the group consisting of metal sulphate hydrates; disodium tetraborate decahydrate; a double salt of the formula M+M3+(SO4)2.12H2O wherein M stand for a metal cation and M+ and M3+ are different; sodium carbonate decahydrate; sodium metasilicate; potassium silicate; ferroso-ferric chloride; dibasic sodium phosphate; potassium pyrophosphate; alumina trihydrate and magnesium orthophosphate.
A building component according to claim 18 wherein the inorganic hydrogel is a silica gel formed from sodium silicate.
PCT/IB2001/001253 2000-07-14 2001-07-13 Method of increasing the heat insulating capacity of a material WO2002008139A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2001269366A AU2001269366A1 (en) 2000-07-14 2001-07-13 Method of increasing the heat insulating capacity of a material

Applications Claiming Priority (8)

Application Number Priority Date Filing Date Title
ZA2000/3552 2000-07-14
ZA200003552 2000-07-14
ZA2000/3739 2000-07-25
ZA200003739 2000-07-25
ZA2001/0644 2001-01-23
ZA200100644 2001-01-23
ZA2001/4315 2001-05-25
ZA200104315 2001-05-25

Publications (2)

Publication Number Publication Date
WO2002008139A2 true WO2002008139A2 (en) 2002-01-31
WO2002008139A3 WO2002008139A3 (en) 2002-04-18

Family

ID=27506106

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2001/001253 WO2002008139A2 (en) 2000-07-14 2001-07-13 Method of increasing the heat insulating capacity of a material

Country Status (2)

Country Link
AU (1) AU2001269366A1 (en)
WO (1) WO2002008139A2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005052088A1 (en) * 2003-11-24 2005-06-09 Oztech Pty Ltd As Trustee Of The Oztech Trust Fire mitigation
WO2012019578A3 (en) * 2010-05-26 2012-04-26 Kerapor Gmbh Fire-retarding materials mixture
US9268121B2 (en) 2010-12-01 2016-02-23 Koninklijke Philips N.V. Sensor device with double telecentric optical system
CN110510904A (en) * 2019-08-30 2019-11-29 中海润达新材料科技有限公司 A kind of additive and its application
US11404854B2 (en) 2017-06-21 2022-08-02 C-Ling Limited Pull-in head assembly
US11411376B2 (en) 2017-06-21 2022-08-09 C-Ling Limited Pull-in head assembly
US11418016B2 (en) 2017-06-21 2022-08-16 C-Ling Limited Pull-in head assembly
US11473563B2 (en) 2016-09-28 2022-10-18 C-Ling Limited Annular seal member locatable against a wall element of an offshore structure

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1474167A (en) * 1966-02-10 1967-03-24 Vermiculite Perlite Sa New insulating foamed article and process for its preparation
DE3142096A1 (en) * 1981-10-23 1983-05-11 Chemische Fabrik Budenheim Rudolf A. Oetker, 6501 Budenheim Fire-retarding insulating materials and process for producing them
EP0356320A2 (en) * 1988-08-24 1990-02-28 Daussan Et Compagnie Organic coating for protecting constructions, in particular against fire and heat
DE19525329A1 (en) * 1995-07-12 1997-01-16 Walter Kraemer High temp. resistant fireproof thermal insulation material - based on expanded perlite and aluminium and magnesium-aluminium silicate(s)

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1474167A (en) * 1966-02-10 1967-03-24 Vermiculite Perlite Sa New insulating foamed article and process for its preparation
DE3142096A1 (en) * 1981-10-23 1983-05-11 Chemische Fabrik Budenheim Rudolf A. Oetker, 6501 Budenheim Fire-retarding insulating materials and process for producing them
EP0356320A2 (en) * 1988-08-24 1990-02-28 Daussan Et Compagnie Organic coating for protecting constructions, in particular against fire and heat
DE19525329A1 (en) * 1995-07-12 1997-01-16 Walter Kraemer High temp. resistant fireproof thermal insulation material - based on expanded perlite and aluminium and magnesium-aluminium silicate(s)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005052088A1 (en) * 2003-11-24 2005-06-09 Oztech Pty Ltd As Trustee Of The Oztech Trust Fire mitigation
AU2004293659B2 (en) * 2003-11-24 2010-06-10 Flexiblast Pty Limited Fire mitigation
US7832324B2 (en) 2003-11-24 2010-11-16 Flexiblast Pty Ltd. Fire mitigation
US7861637B2 (en) 2003-11-24 2011-01-04 Flexiblast Pty Ltd Pressure impulse mitigation
WO2012019578A3 (en) * 2010-05-26 2012-04-26 Kerapor Gmbh Fire-retarding materials mixture
US9268121B2 (en) 2010-12-01 2016-02-23 Koninklijke Philips N.V. Sensor device with double telecentric optical system
US11473563B2 (en) 2016-09-28 2022-10-18 C-Ling Limited Annular seal member locatable against a wall element of an offshore structure
US12071926B2 (en) 2016-09-28 2024-08-27 C-Ling Limited Apparatus
US11404854B2 (en) 2017-06-21 2022-08-02 C-Ling Limited Pull-in head assembly
US11411376B2 (en) 2017-06-21 2022-08-09 C-Ling Limited Pull-in head assembly
US11418016B2 (en) 2017-06-21 2022-08-16 C-Ling Limited Pull-in head assembly
CN110510904A (en) * 2019-08-30 2019-11-29 中海润达新材料科技有限公司 A kind of additive and its application

Also Published As

Publication number Publication date
WO2002008139A3 (en) 2002-04-18
AU2001269366A1 (en) 2002-02-05

Similar Documents

Publication Publication Date Title
US12012361B2 (en) Geopolymer cement
US6010565A (en) Foamed material for fireproofing and/or insulating
US4586958A (en) Process for producing a fire-resistant, light-weight construction board
WO2002008139A2 (en) Method of increasing the heat insulating capacity of a material
US20100180797A1 (en) Ceramic Fire Protection Panel and Method for Producing the Same
US4101475A (en) Flame resistant materials and method of making same
JP2002154864A (en) Building material composition
JP2003146775A (en) Decorative building material
CN113242842A (en) Fire-resistant heat-insulating composition, fire-resistant heat-insulating composition slurry, fire-resistant heat-insulating plate, and fire-resistant heat-insulating structure
JP2001113616A (en) Noncombustible fire-proof heat insulating panel
CN114174239B (en) High fire resistant building board and method for producing high fire resistant building board
Elshimy et al. Repurposing carbonate-based waste for producing an innovative binder: optimization and characterization
JP3373883B2 (en) Light refractory structural material of zeolite-magnesia system
WO2002090292A2 (en) Method of making a finished product from a feedstock, an alkaline earth metal oxide or hydroxide, and a thermosetting resin
WO2022004749A1 (en) Fire-resistant heat insulation composition, fire-resistant heat insulation composition slurry, fire-resistant heat insulation board, and fire-resistant heat insulation structure
JP2004277188A (en) Composition for building material, and moisture-controlling building material
WO2022004750A1 (en) Fire-resistant insulating composition, fire-resistant insulating composition slurry, fire-resistant insulating board, and fire-resistant insulating structure body
KR20030029419A (en) Fireproof Reinforced Materials for Building Construction and Preparation Method Thereof
JPH081854A (en) Refractory board
JPH06321599A (en) Refractory coating material
WO2002047900A1 (en) Method of making a fire resistant building panel
JP2000034180A (en) Production of inorganic foam
JPH10195224A (en) Inoganic and organic composite foam and its production
WO2002100796A1 (en) Method of making a fire resistant finished product
US20240157675A1 (en) Gypsum Panel Containing Additives for Improved Fire Resistance

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
AK Designated states

Kind code of ref document: A3

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A3

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP