GB1585104A

GB1585104A - Vermiculite foam

Info

Publication number: GB1585104A
Application number: GB14764/76A
Authority: GB
Original assignee: Imperial Chemical Industries Ltd
Current assignee: Imperial Chemical Industries Ltd
Priority date: 1976-04-12
Filing date: 1976-04-12
Publication date: 1981-02-25
Also published as: BE853367A; ZA772095B; SE7704045L; NL174452C; DE2716152C2; AU2414477A; JPS52128918A; JPS5915110B2; NL7703870A; NO771224L; NO145688C; SE426313B; DK158377A; AU515006B2; DE2716152A1; FR2348171B1; CA1091862A; NO145688B; NO810499L; FI771104A

Description

(54) VERMICULITE FOAM (71) We, IMPERIAL CHEMICAL INDUSTRIES LIMITED, Imperial Chemical House, Milibank, London SW1P 3jF a British Company do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: This invention relates to inorganic foams and in particular to rigid foams of minerals.

According to the present invention there is provided a rigid foam comprising an inorganic cellular structure composed of lamellae od vermiculite.

Vermiculite is a phyllosilicate mineral i.e.

one having a layer structure. Vermiculite may be swollen by the action of aqueous salts and thereafter the structure broken down (i.e.

delaminated) by mechanical action into extremely thin lamellae. Other phyllosilicate minerals for example hydrobiotites, or chloritevermiculites also contain a substantial proportion of vermiculite layers and these also may be exfoliated in the same or similar manner. These minerals which contain vermiculite layers also give rise to thin lamellae and it is ro be understood that they are included in the present invention. It is preferred to use the lamellae of vermiculite itself for the formation of the inorganic foam of this invention.

According to a preferred aspect ob the present invention there is provided a rigid foam comprising a cellular structure having the cell walls thereof composed od overlapping mdi- vidual vermiculite lamellae adhering together by mutually attractive forces.

The cellular structure extends continuously and substantially uniformly in all dimensions throughout the volume of the foam formed.

The overlapping lamellae constitute the boundary walls od each cell in the cellular structure so that, in the structure as a whole, the individual lamellae are present in all possible orientations with respect to a given plane of reference. Thus, the foam of the preset invention may be distinguished from the heat exfoliated vermiculite granules which have been produced hitherto. In these heated granules a low density form of the mineral is produced wherein, within each granule (which was a separate particle before heat-exfoliation) the layers of the mineral are forced apart during the heating process but remain substantially parallel to one another. Furthermore, such a structure exists only within each granule and does not extend to a continuous structure between granules.This known form of lowdensity vermiculite is not included within the scope of the present invention.

The aforementioned individual lamellae, which may alternatively be termed platelets or flakes, possess for example a small dimen sion o less than 0.5cm, preferably less than 0.05ism, especially less than 0.005jm and have approximately similar length or breadth dimensions of at least a hundred, preferably at least a thousand, times greater than that of the small dimension.

The density of the foams of this invention lies in the range less than 0.5 g/ml and usually less than 0.15 g/ml and for especially "light" foams the density may be for ex ample as low as 0.01 g/ml.

The density may be varied in several different ways, for example by incorporating different amounts of gas into the suspension or by altering the solids content of the suspension. For a low density foam the solids content may be suitably from 5 to 20% by weight whereas if a higher density foam is required the solids content may be increased to 30% w/w or more According to a further aspect of the present invention there is provided a process for producing a rigid vermiculite foam comprising the production of a suspension of vermiculite lamellae in a liquid medium, preferably an aqueous liquid medium, gasification of the suspension to form a froth and removal od the liquid medium from the froth by evaporation.

The swelling and delamination of vermi culite to give aqueous dispersions of vermiculite lamellae has been described in several publications for example UK Patent Specifications Nos. 1,016,385; 1,07b,786 and 1,119,305 and by Baumeister and Hahn "Micron" 7 247 (1976): the procedures dis dosed therein are applicable to the present invention as procedures for producing a suspension of vermiculite lamellae. However for the formation of foams we prefer to have a surface active agent or a foaming agent present in the suspension prior to the gasification of the suspension to form the froth; which term includes an expanded form of the whole suspension.

It is advantageous for the surface active agent or foaming agent to be one which is capable of penetrating the structure of the mineral and thus will swell the mineral and allow delamination to occur. We especially prefer to use a cationic organic salt which is capable of undergoing ion exchange with rhe cations present in the vermiculite layers.

Cationic surface active agents which are especially favoured are the hydrocarbon substituted ammonium group of surfactants. For example the substitution may be of from 1 to 4 hydrogen atoms on the ammonium cation by alkyl, aryl, alicyclic, or heterocyclic groups.

Examples of preferred cationic salts are n-butyl ammonium chloride isobutyl ammonium chloride isoamyl ammonium chloride butyl pyridinium bromide cetyl trimethyl ammonium bromide 2-ethyl hexyl ammonium chloride dodecyl ammonium chloride lysine monohydrochloride ornithine monohydrochloride and polypeptides in cationic form.Other types of foaming agents or foam-producing surfactants may also be employed as additives to the suspension of vermiculite lamellae, as adjuvants to other swelling agents e.g. alkali metal chlorides or in combination with the aforementioned cationic salts, for example long-chain aliphatic alcohols (e.g. cetyl also; hol), alkyl sulphate salts, (e.g. sodium lauryl sulphate) N-acyl sarcosinates and long-chain aliphatic -amine oxides (e.g. oleyl dimethyl amine N-oxide).

An alternative class of foaming agents which may be used with advantage as additives to the suspension of vermiculite lamellae are the protein type foaming agents for example water-soluble proteins (such as albumin or gelatin) or water soluhilised protein derivatives such as hydrolysed soya bean and hydrolysed blood or feathers.

The liquid medium, if aqueous, may contain water-miscible organic liquids for example the lower alcohols or acetone. Alternatively rhe foam may be produced in a non-aqueous medium using suitably modified vermiculites as - described in UK Patent 1,076,786. Our copending UK application No. 41733/79 (Serial No. 1,582,121) describes and claims a process for making a vermiculite suspension using the preferred agents sodium chloride and butyl ammoniuni chloride.

The gasification process may be performed by means of a release of gas or vapour in the suspension of vermiculite lamellae preferably one which is substantially inert to the aqueous suspension for example air, nitrogen, argon, carbon dioxide, a hydrocarbon, chlorocarbon, fluorocarbon or chiorofluorocarbon. The gasification may more conveniently be performed by mechanically entraining the gas in the suspension by rapdd agitation for example by rapid churning or whisking of the suspension.

Alternatively the suspension may be rapidly heated and the foam produced by gasification due either to steam produced by evaporation of water or to liberation od gas dissolved in the sample.

By the term rigid foam we mean a two phase dispersion ob gas in solid, the solid phase being an essentially continuous inorganic cellular structure. Small quantities od organic materials may be present in the foam, which may be either deliberately added or inadvertently present, but the organic material is not fundamental to the cohesion of the cellular structure although it may usefully modçify the properties thereof. On removal od water from an aqueous dispersion od vermiculite lamellae, the lamellae come together to form a coherent film. Accordingly the cell walls of the cellular structure of the present invention derive their mechanical strength largely or wholly from the selfadhesion of the flakes when water is removed.

The resulting structure is a non-brittle foam i.e. under stress the structure may deform without crumbling.

The cellular vermiculite is a useful heatresistant and heat insulating material which may be cast as a foarnfilling for cavities and voids or which may be used as a coating for the outside of materials for example wood or steelwork; in both cases the vermiculite foam acting inter alia as a fire-protective layer. The vermiculite foam may be produced as a slab stock for subsequent fabrication or other lamination. An inner sandwich of vermiculite foam as herein provided, optionally bounded for example by sheets of woodveneer, paper, asbestos, mica or plastic, or by vermiculite sheet, forms useful decorative construction panels: the vermiculite foam may be sandwiched between plaster board or sheets of thermousetting resin e.g. melamine resin. The fore-going structures form useful fire-resistant and/or sound insulating panels for the building industry, panels which may be maintained at temperatures od ca.10000C without disintegration.Sheets of vermiculite foam may be applied as facings to polyure thane foam panels by conventional lamination techniques in order to improve the fire resistance of the polyurethane foam core. The froth i.e. the gasified suspensions before drying may be conveniently used to bond to; gether previously formed vermiculite structurps e.g. sheets or slabs of foam already in dried form and so cement several sheets together and build up larger structures. In a similar way the heatexioliated vermiculite granules may be cemented together by means of the same froth and thus a composite structure is formed consisting of the foam of the present invention as a continuous cement between granules of heatexioliated vermiculite.

For some applications the vermiculite foam may require a water-proofing treatment for example a treatment with ammonia as described in the provisional specification accompanying our copending application (UK Patent Application No. 14551/77).

The invention is illustrated by the following Examples.

Example 1.

1 Kg of vermiculite ore of South Africa origin known as Mandoval micron grade was refluxed in 5 litres of saturated sodium chloride solution for 30 minutes. Excess brine was decanted off and the vermiculite washed in 5 litres of distilled water. This was followed by five separate washings of the solid with one litre aliquots of distilled water on a Buchner filter funnel. The wet cake of vermiculite was returned to the refluxing vessel and refluxed for two hours with 1.25 mole of butyl ammonium chloride made up ta five litres volume with distilled water. After reflux, a washing procedure as described above was carried out during which a rapid expansion of the vermiculite to about six times its original volume occurred.After standing overnight the supernatant liquid was decanted off and the 6 litres od swollen vermiculite ore was divided into two portions of a proximately 3 litres each and each made up to 4 litres with distilled water in a large beaker.

Each suspension was then sheared for one hour using a rotary-bladed mixer dipping into each beaker and working at 6,500 rpm.

The suspension was maintained near to ambient temperature by a spray of cold water to the ouside of each beaker. Air became entrained in the suspension od the lamellae during this process and a froth appeared on the surface of each suspension. The depth of froth increased when the suspension was allowed to stand for 30 minutes and ca.

600 ml of foam was scraped from the suspension in each beaker.

The foam was placed in a mould and dried in a well ventilated oven at 600C. A hard foam of vermiculite having a density of 0.08 g/ml was removed from the mould.

The foam had adopted the permanent shape d the mould and had acquired a skin film of vermiculite over the surface.

The suspension of lamellae was churned at high-speed again for a period of 60 minutes and allowed to stand for a further 30 minutes whereupon a fresh quantity od froth appeared.

The process was repeated several times and thereby several batches of foam were made from the same suspension. These were combined and removed to a mould and dried in the oven to form a solid foam ob density 0.08 g/ml and average cell diameter 0.7 mm.

Example 2.

A sample of ground vermiculite ore from the deposits in North America (Zonolite No. 4) was refluxed for 30 minutes in a saturated solution of sodium chloride and thoroughly washed with several portions of distilled water. The particles were then given a two hour reflux in an aqueous solution of n-butyl ammonium chloride followed again by a thorough washing in distilled water.

During this second washing (which may last conveniently between a few minutes and several hours) a pronounced swelling of the particles occurred to approximately six times their original wet volume. This was then a sample of expanded vermiculite.

The weight ratio of the aqueous suspension of the swellen vermiculite was adjusted by removal of water by filtration until the weight ratio was approximately 10% vermiculite solids to 90% liquid water. The suspension was placed in a high-shear mixer (manufactured by Greaves Limited) which had a blade capable of rotating at 6,500 rpm and the suspension was mechanically milled or macerated for a period of 10 minutes. During this process air was entrained in the suspension and when the rotation of the blade was stopped and the suspension allowed to stand for 5 minutes several inches depth of froth was present above the suspension. The froth was taken off with a knife and spread on a tray.The tray containing the froth was placed in a well-ventilated oven at ca. 600C and the water removed by evaporation, optionally aided by a fan or extractor in the oven. When dry the foam could be removed from the tray as a solid cellular vermiculite structure having a density of less than 0.1 g/ml and average cell diameter of 0.5 mm.

Example 3.

A sample of Zonolite No. 4 vermiculite was treated as described in Example 2 the suspension being milled for 60 minutes. The density od the resultant foam was 0.035 g/ml and the average cell diameter was 0.5 mm.

Example 4.

South African vermiculite was expanded as described in the first paragraph o Example 1. After adjusting the solids content of the swollen vermiculite suspension to 20% w/w it was stirred until homogeneous and subjected to a single pass through a mill od the type known as a "rotor-in-stator" mill, running at a speed ob 20,000 rpm. Before passing into the shearing zone of the mill, air was metered into the suspension at a rate of 10 litre/min. The whole suspension was converted to a thick froth which on standing overnight separated out into a lower liquid layer containing some of the larger sized vermiculite particles and another layer of wet vermiculite froth.The froth (which was ob served to be stable for several weeks in the wet stage) was collected and dried in a wiremesh mould in a well ventilated oven at 800C. A slab of foam of dimensions 12" X 12" X 2" was formed and was found to have the following properties: Density 0.22 g/ml Compressive strength 0.11 MNm-2 Thermal conductivity 0.060 Wm -1K-' % closed cells 12% Average cell diameter 1.5 mm Example 5.

3 Kg of American vermiculite was expanded in a similar manner to that described in the first paragraph of Example 2.

The swollen vermiculite was then divided into 9 batches, each of which was milled for 45 minutes in a Greaves mill, in order to produce suspensions of delaminated vermiculite.

The 9 batches were then combined and the larger particles ob vermiculite removed by passing the suspension through a 50ym sieve.

The resultant "classified" suspension which contained approximately 5% solids by weight, was evaporated on a large heated tray to increase the solids content to 20%. Air was then beaten into the thick suspension using a culinary mixer, using the whisking attachment. An approximately two fold volume increase of the suspension took place and a small bubble size wet foam was produced from the whole suspension. The foam was spread on a heated tray and dried overnight to form a board 6' X 4' X 1/4". The dried foam had the following properties: De?Lsity strength 0.12 g/ml Compressive strength 0.30 MNm-2 Thermal conductivity 0.060 Wm -lK- % closed cells 41% Average cell diameter 0.2 mm Example 6.

3 Kg of South African vermiculite was expanded as described in the first paragraph of Example 1. When the expansion was complete the supernatant water was decanted off and the swollen vermiculite milled in 750 ml aliquots in a domestic liquidiser for 10 minutes. The thick, but pourable suspension was found to have solids content of 20% w/w.

The suspension was foamed using a culinary mixer as described in Example 5. The foam was then dried in an oven at 900C overnight to form slabs of dimensions 24" X 12" X 1/4". Several slabs were laminated using wet froth and a larger slab of dimensions 12" X 12" X 11'' was formed and dried in an oven. The physical properties of the larger slab were measured as Density 0.07 g/ml Compressive strength 0.05 MNm-2 Thermal conductivity 0.048 Wrn -1K-1 % closed cells 6% Average cell diameter 0.5 ram Example 7.

A non-foamed suspension of American vermiculite (20% w/w solids content) was prepared as described in Example 5. In this case the suspension was not aerated but was placed in an oven at 1400C for 3 hours, causing rapid evolution d water vapour which produced a dry foam of density 0.10 g/ml.

Example 8.

170 g of South African vermiculite suspension prepared according to the method described in Example 5 the solids content adjusted to 13% w/w and placed in an "Aerosol" container which was adapted to be pressurised. A mixture of 18 g of dichloro difluoromethane and 12 g of dichloro terrafluoroethane was forced under pressure into the Aerosol can and mixed with the vermiculite paste. Upon activation of the ejection nozzle of the can a wet froth was applied to a tray and dried in air over a period of 24 hours. The rigid foam of vermiculite pro duced was observed to, have a very fine pore size (average diameter of bubbles = 350,us) and a density of 0.05 g/ml.

Example 9.

South African (Mandoval "micron" grade) vermiculite (1 Kg.) was refluxed for 10 hours in a mixture of water (4 1.) manganese dichloride tetrahydrate (130 g.) and concentrated hydrochloric add (0.25 ml.). The plrs duct was washed with water and then made up to a total volume of 20 1. with water.

Hydrochloric acid (75 ml. 1N solution) and hydrogen peroxide (2 1. of 30% solution) were then added and the stirred mixture warmed to 600C for 2 hours whereupon the vermiculite expanded to take up most of the liquid present. The mixture was then cooled, filtered washed with water, and made up to 10 1. with added fresh water. The resulting suspension was divided into 4 equal batches and each sheared for one hour at 6500 rpm in a 5 1. vessel with a Greaves H5-Series mixer (Mark III). The combined suspension was then diluted to 16 1. with water and classified by passage through a sieve od aperture size 50pm to give a vermiculite suspen sion containing 2.9 % by weight of solids.

(All water added was distilled).

The concentration of the suspension was then increased to 20% by weight by evapora tion of water by the application of heat, the mixture was cooled and a protein surfactant known commercially as "Nicerol" was then added at a concentration of 10% by volume relative to the weight of the solid vermiculite and portions of the mixture beaten in a culin- ary mixer to form a foam. The foam when dried in a well-ventilated oven at 900C had a density of 0.1 g/ml.

Example 10.

1 Kg. of South African vermiculite was refluxed in a 20% w/w aqueous solution of lithium chloride for 2 hours and after thorough washing in a Buchner funnel and standing overnight in distilled water, an eight-fold volume expansion ob the original ore took place. The mixture of expanded ore and water (10% w/w of ore) was then milled for 1 hour. The larger particles d vermiculite were then removed by filtration through a SOMm sieve and the concentration of the suspension adjusted to 20% w/w by evapora- tion.A protein surfactant known commercially as "Nicerol" at a concentration ob 10% by volume relative to the weight od vermiculite was then added and portions of the mixture beaten in a culinary mixer to form a foam. The foam when dried in a well ven dilated oven at 900C had a density of 0.1 g/ml.

Example 11.

A dried foam based on North American vermiculite was prepared as described in Example 4 and found to have an average size od 3.00mum and a density of 0.01 g/ml.

Example 12.

A sample of wet foam as prepared in Example 6 was blended with granules od heat expanded vermiculite such that in the resul tant blend the wet foam occupied 34% of the total volume and the granules 66% of the total volume. The blend was dried in an oven at 900C. The resultant composite structure had a density of 0.22g/ml and a compressive strength of 0.12 MNm Example 13.

A slab of foam ob dimensions 62 mm X 135 mm X 4 mm cut from the foam produced in Example 5 having a density of 0.12 g/ml was placed in a furnace at 10000C for 10 minutes. On removal from the furnace the slab was observed not to have distorted ar all visibly as a result of the intense heat, the resultant dimensions being 61 mm X 134 mm X 4 mm. The density decreased to 0.09 g/ml and the compressive strength was 0.22 MNm-2.

These results demonstrate that the foams od this invention resist heat well and therefore can be used as a fire-protective material because they have good dimensional stability with little loss in compressive strength.

WHAT WE CLAIM IS: 1. A rigid foam comprising an inorganic cellular structure composed of lamellae of vermiculite.

2. A rigid foam comprising a cellular structure having the cell walls thereof composed of overlapping individual vermiculite lamellae adlhering together by mutually attractive forces.

3. A rigid foam as claimed in daim 1 or, claim 2 wherein the lamellae possess a smallest dimension not greater than 0.5 ,um.

4. A rigid foam as claimed in claim 3 wherein the lamellae have smallest dimension not greater than 0.05 ssm.

5. A rigid foam as claimed in claim 3 or claim 4 wherein the lamellae have length or breadth dimensions of at least one hundred times the size of the smallest dimension.

6. A rigid foam as daimed in claim 5 wherein the lamellae have length or breadth dimensions of at least one thousand times the size of the smallest dimension.

7. A rigid foam as claimed in any one of the preceding claims formed into a con tinuous and substantially uniform sheet or slab of foam as hereinbefore defined.

8. A foam as claimed in any one of the preceding claims having a density not greater than 0.5 g/ml.

9. A foam as claimed in claim 8 and having a density not greater than 0.15 g/ml.

10. A process for the production of a rigid foam of vermiculite comprising the gasifiea- tion of a suspension of vermiculite lamellae in a liquid medium to form a froth and re moval of the liquid medium from the froth by evaporation.

11. A process as claimed in claim 10 for the production of a rigid foam of vermiculite comprising the production of a suspension of vermiculite lamellae in a liquid medium, gasi fication of the suspension to form a froth and removal of the liquid medium from the froth by evaporation.

12. A process as claimed in claim 10 or 11 in which the liquid medium is aqueous.

13. A process as claimed in claim 10, 11 or 12 wherein the gasification is performed by entraining gas in the suspension by rapid agitation.

14. A process as daimed in claim 13 wherein the gasification is performed by whisking or beating the whole suspension into a froth.

15. A process as claimed in claim 10 or

**WARNING** end of DESC field may overlap start of CLMS **.

Claims

**WARNING** start of CLMS field may overlap end of DESC **. was then diluted to 16 1. with water and classified by passage through a sieve od aperture size 50pm to give a vermiculite suspen sion containing 2.9 % by weight of solids. (All water added was distilled). The concentration of the suspension was then increased to 20% by weight by evapora tion of water by the application of heat, the mixture was cooled and a protein surfactant known commercially as "Nicerol" was then added at a concentration of 10% by volume relative to the weight of the solid vermiculite and portions of the mixture beaten in a culin- ary mixer to form a foam. The foam when dried in a well-ventilated oven at 900C had a density of 0.1 g/ml. Example 10.

Example 11.

Example 12.

15. A process as claimed in claim 10 or

claim 11 wherein the gasification, is performed by intimate mixing of the suspension with a volatile liquid and evaporating the liquid in the suspension.

16. A process as claimed in claim 10 or claim 11 wherein the gasification is produced by rapidly heating the suspension.

17. A process as claimed in any one of the claims 10-16 wherein the suspension is classified by the removal of the coarser particles of vermiculite from the suspension prior to the gasification.

18. A process as claimed in any one ob claims 10-17 wherein there is present in the suspension d vermiculate lamellae a surface active agent or foaming agent which is a cationic organic salt.

19. A process as claimed in any one of claims 10-18 wherein a foaming agent or surface active agent is added to the suspension od vermiculite lamellae prior to gasification.

20. A process as claimed in any one of claims 10 to 19 wherein the suspension of vermiculite lamellae is produced by shearing a suspension of swollen vermiculite in water.

21. A process as claimed in claim 20 wherein the suspension of swollen vermiculite is the product od treating vermiculite ore with a solution in water of butyl ammonium chloride and allowing the treated ore to swell in water.

22. A process as claimed in daim 20 wherein the suspension of swollen vermiculite is the product of treating vermiculite ore with a saturated aqueous sodium chloride solution under reflux conditions then with aqueous butyl ammonium chloride solution also under reflux and allowing the treated ore to swell in water.

23. A process as claimed in claim 10 substantially as described herein with reference to and as shown in any one of the foregoing examples.

24. A process as claimed in any one of claims 10-23 wherein during evaporation the foam is contacted with previously formed vermiculite structures, preferably in the form of rigid foam or exfoliated granules, in order to cement the solid vermiculite structures together.

25. A shaped article comprising a foam as claimed in any one of claims 1-9.

26. A shaped article as claimed in claim 25 consisting of a slab of foam having a skin of vermiculite over a substantial part of the surface of the slab.

27. A shaped article as claimed in claim 25 and consisting of a laminated sheet or panel having a slab ob vermiculite foam laminated to a sheet, film or slab of an organic polymer or plastic.

28. A shaped article as claimed in claim 27 comprising a laminate of polyurethane foam with a vermiculite foam.

29. A polyurethane foam panel faced on at least one side with a coating of a foam as claimed in any one of claims 1-9.

30. A shaped article as claimed in claim 25 wherein a slab of vermiculite foam is sandwiched between two facing sheets or boards of a type conventionally used in the building industry.

31. A method of rendering articles fire resistant by applying to the exterior surface of the article a coating of a vermiculite foam as claimed in any one of the claims 1-9.