Porous particulate materials

Abstract: A particulate porous material suitable for use as a high surface area column packing material comprises particles substantially all of which are not smaller than 5 micrometres and not larger than 1 millimetre in diameter, and each particle consists predominantly of an open, three-­ dimensional matrix of crystals of mullite, which are prefer­ ably substantially uniform in size and define between them interconnecting pores having a width in the range of from 5nm to about 2µm. The particles can be coated with a reactive layer. There is also disclosed a process for produc­ ing the particulate porous material wherein a particulate product comprising particles substantially all of which are between 5 micrometres and 1 millimetre in diameter and consisting predominantly of a mixture of mullite crystals and silica is treated with a concentrated aqueous solution of an alkali metal hydroxide at a temperature of at least 50°C; and the treated particulate product is then washed, dewatered and dried.

Description: This invention relates to particulate porous materials and, more particularly but not exclusively, is concerned with such materials which are suitable for use as high surface area column packing materials, and with a process for preparing the same. Mullite is an aluminosilicate material which exists in the form of needle-shaped crystals: it has a variable chemical composition but is generally represented by the formula 3Al 2 O 3 .2SiO 2 . Although mullite occurs naturally, it is usually obtained by heating bauxite with clay or sillimanite. It is presently used as a refractory. EP―A―0130734, relevant under Article 54(3) EPC, relates to porous mullite articles obtained by calcining preformed bodies of clay to form mullite and silica and removing silica from the mullite by leaching. AU―B―22146 relates to a method of producing synthetic mullite which has good refractoriness under load and good thermal shock resistance. Chemical Abstracts, Vol. 98, No. 14, April 1983, page 143, No. 109877, Columbus, Ohio, U.S. relates to the preparation of very reactive premullite from kandites. A natural clay of the kandite group is heat-treated at a temperature of about 900°C to 1100°C to form a mixture of premullite and amorphous SiO 2 , which is treated with an alkali solution having a strength greater than 5% to dissolve the amorphous SiO 2 . According to one aspect of the present invention there is provided a particulate porous material wherein substantially all the particles of the material are not smaller than 5 micrometres and not larger than 1 millimetre in diameter and wherein each particle consists predominantly of an open, three-dimensional matrix of crystals of mullite which are substantially uniform in size and define between them interconnecting pores having a width in the range of from 5 nanometres to about 2 microns. In embodiments of this invention, each particle may be in the form of a cellular body. The cellular body may be, for example, a spherical hollow particle or a rigid foam. The particulate porous material of the invention may be used inter alia as a packing material for a chromatographic or ion exchange column, or for performing biochemical separations. In order to be suitable for the above applications the particulate material should have a high proportion of interconnected voidage of sufficient width that large molecules, such as biological and synthetic polymer molecules, can penetrate easily and rapidly into the particules. Thus, the width of the pores should vary from about 5 nanometres to 2 micrometres. It is also important that all or substantially all of the particles are not smaller than 5 micrometres, in order to ensure that a column packed with the material has a good flow velocity, and not larger than 1 millimetre, in order to ensure that a column packed with the material has a good surface area per unit weight. It is also desirable that the exposed surface of the particles should be easily treated with a reactive layer for the purpose of chromatography or ion exchange. Such a reactive layer may be hydrophilic or hydrophobic or may comprise a mixture of hydrophilic and hydrophobic groups. The porous particulate material should also preferably have good mechanical strength, especially good resistance to crushing and abrasion; it should be resistant to chemical attack by both alkalies and acids, and ideally it should also be able to withstand elevated temperatures and thermal shock. The particulate porous material of the present invention meets these requirements. It has also been found that the particulate porous material of the invention can be used as a support for enzymes or as a filler for paper, paints, plastics or rubber compositions According to another aspect of the invention there is provided a process for preparing a particulate, porous material which process comprises (a) preparing a particulate product comprising particles substantially all of which are between 5 micrometres and 1 millimetre in diameter and consist predominantly of a mixture of mullite crystals and silica by heat-treating an aluminosilicate material having a SiO 2 .Al 2 O 3 molar ratio of at least 0.75:1 at a temperature in the range of from 1000°C to 1800°C; (b) treating the particulate product formed in (a) with a concentrated aqueous solution of an alkali metal hydroxide at a temperature of at least 50°C whereby the silica is removed to leave mullite crystals which are substantially uniform in size and define between them interconnecting pores having a width in the range of from 5 nanometres to 2 micrometres; (c) washing the alkali metal hydroxide-treated particulate product formed in (b) until the washing medium is substantially free of silicate and alkali metal ions; and (d) dewatering and drying the washed product obtained in (c) to obtain the desired particulate porous material. It is advantageous to prepare the aluminosilicate starting material for heat treating at a temperature in the range of from 1000°C to 1800°C in such a way that the heat-treated mixture of mullite crystals and silica already has an open or porous structure This may be achieved by spray drying an aqueous suspension of the aluminosilicate starting material(s) to form dry particles in the form of hollow spheres or by preparing a foam from an aqueous suspension of the aluminosilicate starting material(s) and applying heat to set the foam. Suitable aluminosilicate starting materials include kyanite, sillimanite, andalusite, all of which can be represented by the chemical formula Al 2 O 3 .SiO 2 ; dumortierite which can be represented by the chemical formula 8Al 2 O 3 .B 2 O 3 .6SiO 2 .H 2 O; clay minerals of the kandite group which can be represented by the chemical formula Al 2 O 3 .2SiO 2 .2H 2 O; and pyrophillite which can be represented by the chemical formula Al 2 O 3 .4SiO 2 .H 2 O. Other possible aluminosilicate starting materials include topaz, pinite, illite and clay minerals of the smectite class. It is also possible to use as the aluminosilicate starting material a mixture of an alumina rich material and a silica-rich material, a chemically precipitated aluminosilicate or a mixture of substantially pure alumina and silica, provided that the molar ratio SiO 2 :Al 2 O 3 is at least 0.75:1, and preferably at least 1:1 in each case. We have found clay minerals of the kandite class, namely kaolinite, dickite, nacrite and halloysite to be especially suitable, and in particular kaolin clay which consists predominantly of kaolinite. In some cases it is advantageous to treat the starting material before heat treatment with an aqueous solution containing transition metal cations, for example Cu ++ or Mn ++ ions. It has been found that heat treatment of a starting material which contains transition metal cations produces mullite crystals in a more finely divided form with the result that the particulate porous, material finally produced has a greater number of pores with a smaller average width. The aluminosilicate starting material may be heat-treated by the process known as soak calcination in, for example, a tunnel kiln, in which case the starting material is exposed to a temperature in the range from 1000°C to 1800°C for at least 1 hour. Preferably, the starting material is heat treated at a temperature in the range from 1350°C to 1600°C for a time in the range of from 5 hours to 24 hours. After heat-treatment by soak calcination the mixture of mullite crystals and silica is comminuted and subjected to one or more particle size separations by sieving, air classification and/or centrifugal or gravitational sedimentation. Alternatively, the aluminosilicate starting material may be flash calcined by injecting the starting material, in a finely divided form, for example in powder or spray dried form, into a fluidised bed or a vortex of hot gases maintained at a temperature in the range from 1000°C to 1800°C for a time of as little as a few seconds. After heat-treatment by flash calcination the product may already consist of particles having sizes within the range of from 5 micrometres to 1 millimetre and comminution and particle size separation steps may not be necessary. If in step (b) the silica in the heat-treated mixture of mullite crystals and silica is to be readily soluble in the concentrated aqueous solution of an alkali metal hydroxide the aluminosilicate starting material should preferably contain from 1.5% to 2.5% by weight of M 2 O where M is sodium and/or potassium. If the starting material contains less than this amount of M 2 O, the M 2 O content may be increased by adding an appropriate quantity of an M 2 O-containing mineral, such as feldspar. Preferably, the particulate product of step (a) has a narrow range of particle sizes. For example an especially advantageous product comprises particles substantially all of which are between 10 microns and 100 microns in size. In step (b) the alkali metal hydroxide is most conveniently sodium hydroxide and the molarity of the alkali solution is preferably at least 3M. Advantageously, the reaction between the particulate product of step (a) and the alkali metal hydroxide solution is performed at a temperature between 80°C and the boiling point of the alkali metal hydroxide solution. The purpose of step (b) is to dissolve substantially completely from the mixture of mullite and silica, the silica component which is generally present in a glassy form. After the silica has been removed by dissolution each particle consists predominantly of mullite needles joined together in the form of a three-dimensional lattice which has high proportion of interconnecting voidage, the passages of which are relatively wide in relation to the width of the mullite needles. In step (c) the alkali-treated particulate product of step (b) is preferably washed first with an alkaline solution weaker than that used in step (b) and then repeatedly with water until the washing medium is substantially free of silicate and alkali metal ions. The alkaline solution used in this washing procedure preferably has a molarity of 1 M or less. The dry particulate product obtained on carrying out step (d) is found to have good mechanical properties when packed into a column for the purpose of, for example, chromatography or ion exchange. In particular the particles are resistant to crushing and abrasion and can withstand a high differential pressure between one end of the column and the other when a liquid is pumped through the column. Since the melting point of mullite is about 1810°C the particulate product can be subjected to high temperatures for long periods without fusing or sintering, and it has been found that the material has good resistance to thermal shock, being able to withstand repeated quenching from 1200°C to room temperature with no deleterious effect on its structure. The particulate porous material is also able to withstand prolonged exposure to strong acids of pH 1 and strong alkalies of pH 14. Of the known comparable materials silica is soluble in strongly alkaline solutions and alumina and clays are attacked by strong acids. The particulate porous material of the invention is readily coated with a reactive layer for the purposes of affinity chromatography or ion exchange, or biochemical separations. Examples of materials which can be coated on to the particulate porous material to form reactive layers include polyacidic organic bases such as polyethyleneimines, which will form bonds directly with the surface of the mullite crystals, possess both hydrophobic and hydrophilic groups and have anion exchange properties which are useful in biological applications such as treating proteins. Other materials which can be coated directly on to the mullite crystals include thermoplastic materials such as polystyrene and polysaccharides. An example of a substituted polysaccharide material which has been found to form a useful reactive layer is "DEAE Dextran" which is a dextran substituted with pendant diethylamine ethyl groups: this provides a hydrophilic organic layer with anion exchange properties. The surface of the particulate porous material may be rendered hydrophobic, and be given an overall positive charge, by applying a coating of a quaternary ammonium compound which has at least one hydrocarbon radical with from 10 to 24 carbon atoms. Some materials can only be used to form reactive layers after the mullite crystals have first been coated with a bonding agent. Suitable bonding agents are substituted silanes, especially those comprising at least one hydroxy, hydroxyalkyl or alkoxy group for bonding with hydroxyl groups on the surface of the mullite crystals and at least one aminoalkyl diazo or haloalkyl group for bonding with the material of the desired layer. An example of a suitable substituted silane is 3-aminopropyltriethoxysilane. Reactive layer materials which will form bonds with the substituted silane include nucleic acid bases, such as adenine which is very useful for the concentration and separation of nucleic acids, and polysuccinimide which is very suitable for affinity chromatography and for immobilising enzymes. The particulate porous material of the invention is also useful as a filler for plastics materials or for natural or synthetic rubber compositions. The high portion of interconnected voidage provides good mechanical keying between the polymeric material and the particulate material. The particulate material may, if desired, be pre-coated with a layer of substituted silane, such as those described in British Patent Specification No. 2067535, in order to improve the chemical bonding between the polymeric material and the filler. The particulate porous material of the invention is also useful as a filler for paper since the fine pores of the particulate material trap air and this increases the scattering of light and improves the whiteness of a composition in which the porous material is incorporated as a filler. The invention is illustrated by the following Examples. Example 1 a) A Cornish kaolin clay having a particle size distribution such that 36% by weight consisted of particles having an equivalent spherical diameter smaller than 2 microns and 30% by weight consisted of particles having an equivalent diameter larger than 10 microns, and containing 1.7% by weight of K 2 O, was fired in a tunnel kiln under conditions such that it was exposed to a temperature of 1500°C for 8 hours. After cooling, the calcined material, which comprised mullite crystals set in a glassy silica phase, was crushed and ground and the comminuted material was subjected to particle size separation by sieving. The material passing a No. 200 mesh British Standard sieve (nominal aperture 76 microns) was selected for further processing and was subjected to air classification to remove substantially all particles smaller than 10 microns. b) A sample of this particulate material was then boiled with 100 ml of 5 M sodium hydroxide for 1 hour. The liquor was then removed using a centrifuge. c) The solid material was washed with water, the washings also being removed by centrifuge. d) The washed solid material was then dried in an oven at 60°C and the dry cake milled in a Janke and Kunkel laboratory analytical mill. Atomic absorption analysis of the liquor and washings showed that the amount of silica removed was 26.4% by weight of the total weight of the heat-treated kaolin (the theoretical proportion of the glassy silica phase in heat-treated kaolin is 38.6% of the total weight). Scanning electron micrographs (see the accompanying Figures 1 and 2) showed that the particles had a surface consisting of an exposed three dimensional matrix of mullite crystals. Example 2 Further 15 g samples of the particulate heat-treated kaolin prepared as described in Example 1 were boiled with 250 ml of 5 M sodium hydroxide solution for varying lengths of time. In each case the liquor was separated and the alkali-treated material washed, dried and comminuted as described in Example 1. In each case the liquor and washings were subjected to atomic absorption analysis for silicon and the amount of silica removed, expressed as a percentage of the total weight of the heat-treated kaolin, was calculated in each case. The results obtained are set forth in Table 1 below:― Treatment time (hours) Silica removed (% by weight) ½ 16.9 1 25.3 2 26.6 4 27.8 It can be seen that a significant proportion of the glassy silica phase was removed on boiling for only ½ hour and there is little advantage to be obtained by prolonging the time of boiling beyond 1 hour. Example 3 Further 15 g samples of the particulate heat-treated kaolin prepared as described in Example 1 were boiled for 1 hour with 250 ml of sodium hydroxide solutions of varying molarity. In each case the liquor was separated and the alkali-treated material washed, dried and comminuted as described in Example 1. In each case the liquor and washings were subjected to atomic absorption analysis for silicon and the weight of silica removed, expressed as a percentage of the total weight of the heat-treated kaolin, was calculated in each case. The results obtained are set forth in Table 2 below:― Molarity of NaOH solution Silica removed (% by weight) 1 M 11.5 3 M 21.2 5 M 25.3 7 M 25.8 These results show that the molarity of the sodium hydroxide is preferably at least 3 M but that there is little advantage in increasing the molarity above 5 M. Example 4 Further 15 g samples of the particulate, heat-treated kaolin prepared as described in Example 1 were contacted for 1 hour with 250 ml of 5 M sodium hydroxide solution at varying temperatures. In each case the liquor was separated and the alkali-treated material washed, dried and comminuted as described in Example 1. In each case the liquor and the washings were subjected to atomic absorption analysis for silicon and the weight of silica removed, expressed as a percentage of the total weight of the heat-treated kaolin, was calculated in each case. The results obtained are set forth in Table 3 below:― Treatment temperatures °C Silica removed (% by weight) 25 0.07 50 1.3 75 4.7 100 25.3 These results show that it is important that the particulate heat-treated kaolin is contacted with sodium hydroxide solution at a temperature close to the boiling point of the solution. Example 5 a) A sample of the same kaolin clay as was used in Example 1 was vigorously mixed with sufficient water to form a suspension containing 65% by weight of dry kaolin and 0.6% by weight, based on the weight of dry kaolin, of tetrasodium pyrophosphate as a dispersing agent. The resultant suspension was then diluted with water to a solids content of 40% by weight and was beaten for 10 minutes in a household food mixer in the presence of 1% by weight, based on the weight of dry kaolin, of the surfactant n-octylamine phosphate. The resultant wet foam was transferred to an open pan and dried for 16 hours at 80°C in an oven and then heat-treated for 4 hours at 1000°C to ensure that the foam was well set. The substantially rigid foam was fired in a tunnel kiln under conditions such that it was exposed to a temperature of 1500°C for 8 hours. After cooling, the calcined material was lightly crushed and the comminuted material was subjected to particle size separation by sieving on a No. 200 mesh British Standard sieve (0.076 mm). b) 1 g of the particulate material passing through the sieve was boiled with 100 ml of 5 M sodium hydroxide for 1 hour. The liquor was removed using a centrifuge. c) The sample was washed with water, the washings also being removed by centrifuge. d) The washed sample was then dried in an oven at 60°C and the dry cake milled in a Janke and Kunkel laboratory analytical mill. The product was tested as described in Example 8 below. Example 6 A sample of the same kaolin clay as was used in Example 1 was vigorously mixed with sufficient water to form a suspension containing 62% by weight of dry kaolin and 0.6% by weight, based on the weight of dry kaolin, of tetrasodium pyrophosphate. The resultant suspension was then fed at a rate of approximately 1 litre per minute to a laboratory spray dryer operating at an inlet temperature of 380°C and an outlet temperature of 175°C. The dried product which was in the form of hollow spheres of substantially uniform diameter of about 50 microns was fired in a tunnel kiln under conditions such that it was exposed to a temperature of 1500°C for 8 hours. After cooling, the calcined material was lightly crushed to separate the spheres which had become fused together during the firing and the crushed material was divided into two portions A and B. Portion A was reserved for further testing as described in Example 8 below, while 1 g of Portion B was treated with sodium hydroxide under identical conditions to those described in Example 5 and the treated material was centrifuged, washed, dried and milled in the same way. Example 7 The particulate mullite product of Example 1 was mixed with water to form a suspension containing 10% by weight of dry solids and portions of this suspension were mixed with varying quantities of an aqueous solution, at a temperature of 60°C, containing 10% by weight of the quaternary ammonium compound, dimethyl di-(hydrogenated tallow) ammonium chloride (2M2HT). The mixture was stirred at a temperature of 60°C for half an hour after which the suspension was filtered and the cake washed with water and dried. 0.5 g of each of the dried products, which consisted of particulate mullite coated with varying amounts of 2M2HT, was mixed with 50 ml of deionised water for 5 minutes in an ultrasonic bath to ensure homogeneity of the suspension. The suspension was then further diluted with deionised water to a solids content of 0.05% by weight and a sample of the very dilute suspension was tested under the microscope in a thin rectangular electrophoretic cell with a potential difference of 80 V between the two electrodes. The mobility µ E of particules in the suspension, or the velocity in cm.s -1 under a potential gradient of 1 V.cm -1 , was determined by measuring the time in seconds taken for a particle to traverse one square of the grid of the microscope. Twenty measurements of the time were made for each sample of suspension, the polarity of the electrodes being reversed after each measurement, and the mean value of the time was used to calculate the value of the velocity V E of the particles. The mobility of the particles was calculated from the formula: µ E = V E X where X is the potential gradient in V.cm -1 . The zeta potential, or the difference in potential between the immovable liquid layer attached to the surface of a solid phase and the movable part of the diffuse layer in the body of the liquid, was then calculated from the formula: ζ= 4πηµ E ε where η is the viscosity at the operating temperature, and ε is the dielectric constant, of the aqueous medium. The results are set forth in Table 4 below: Particulate material Meq. 2M2HT per 100 g of particulate material Mobility (cm.s -1 ) Surface charge Zeta potential (mV) Ex. 1―not NaOH treated 0 4.50 - -58.1 Ex. 1―NaOH treated 0 3.43 - -44.3 Ex. 1―NaOH treated 1 3.24 - -41.9 Ex. 1―NaOH treated 3 3.03 - -39.1 Ex. 1―NaOH treated 5 2.42 - -31.9 Ex. 1―NaOH treated 8 5.03 + +64.9 Ex. 1―NaOH treated 10 5.01 + +64.6 These results show that the negative charge on the surface of the particulate material is neutralised when the quantity of 2M2HT adsorbed on the surface has a value between 5 and 8 milliequivalents of 2M2HT per 100 g of the particulate material. The surface of the particulate material was found to have a significantly hydrophobic nature when the quantity of 2M2HT adsorbed with 5 milliequivalents per 100 g of particulate material. Example 8 The degree of adsorption of protein to the surface of various particulate materials in accordance with the invention was investigated by adding 1 g of particulate material to 15 ml of an aqueous solution containing 100 ppm of myoglobin and subjecting the mixture to mild agitation in the form of a gentle tumbling action for 18 hours to allow equilibrium to be reached. The mixture was then allowed to stand for 5 hours and centrifuged for 5 minutes at 3000 rpm to separate the particulate material from the solution of unadsorbed protein. The protein content of the initial solution and of the solution of unadsorbed protein separated by the centrifuge were determined by ultra violet spectrophotometry and the difference between the two measurements gave a measure of the quantity of myoglobin in milligrams which was adsorbed by 1 g of particulate material. In most cases the specific surface area of the particulate material was also determined by the B.E.T. nitrogen adsorption method. The results obtained are set forth in Table 5 below. Particulate material Specific surface area (m 2 g -1 ) Myoglobin adsorbed (mg.g -1 ) Ex. 1.―not NaOH treated 0.3 0.26 Ex. 1.―NaOH treated 0.8 0.57 Ex. 7―5 meq. 2M2HT per 100 g ― 0.9 Ex. 5.―foamed 5.1 1.2 Ex. 6. Portion A―spray dried, not NaOH treated 0.9 0.2 Ex. 6. Portion B―spray dried, NaOH treated 1.5 0.7 Ex. 6. Portion B coated with 5 meq. 2M2HT per 100 g ― 0.95 These results show that both the specific surface area and the capacity to adsorb protein are increased when the aluminosilicate material consisting predominantly of mullite crystals and silica is treated with concentrated sodium hydroxide solution to dissolve at least part of the silica. A further increase is observed when the aluminosilicate material is prepared from a foamed or spray dried starting material. A still further increase in the capacity to adsorb protein may be achieved by adsorbing about 5 meq. of 2M2HT on the surface of the alkali treated aluminosilicate material thus rendering the surface hydrophobic.

Claims: A particulate porous material which is resistant to crushing and abrasion wherein substantially all the particles of the material are not smaller than 5 micrometres and not larger than 1 millimetre in diameter and wherein each particle consists predominantly of an open, three-dimensional matrix of needle-shaped crystals of mullite which are substantially uniform in size and define between them interconnecting pores having a width in the range of from 5 nanometres to about 2 microns. A particulate porous material as claimed in claim 1, wherein the particles are coated with a layer of an organic material containing hydrophilic groups, hydrophobic groups or a mixture of hydrophilic and hydrophobic groups. A particulate porous material according to Claim 1 or 2, wherein each particle is in the form of a cellular body. A particulate porous material according to Claim 1, 2 or 3, wherein the cellular body is a spherical hollow particle. A particulate porous material according to Claim 1, 2 or 3, wherein the cellular body is a rigid foam. A particulate porous material according to Claim 1, 2, 3, 4 or 5, wherein substantially all of the particles of the material are not smaller than 10 micrometres and not larger than 100 micrometres. A process for producing a particulate porous material which process comprises (a) preparing a particulate product comprising particles substantially all of which are between 5 micrometres and 1 millimetre in diameter and consisting predominantly of a mixture of mullite crystals and silica by heat-treating an aluminosilicate material having a SiO 2 .Al 2 O 2 molar ratio of at least 0.75:1 at a temperature in the range of from 1000°C to 1800°C; (b) treating the particulate product formed in (a) with a concentrated aqueous solution of an alkali metal hydroxide at a temperature of at least 50°C whereby the silica is removed to leave mullite crystals which are substantially uniform in size and define between them interconnecting pores having a width in the range of from 5 nanometres to 2 micrometres; (c) washing the alkali metal hydroxide-treated particulate product formed in (b) until the washing medium is substantially free of silicate and alkali metal ions; and (d) dewatering and drying the washed product obtained in (c) to obtain the desired particulate porous material. A process according to claim 7, wherein the mixture of mullite crystals and silica is formed by heat-treating an aluminosilicate material having a SiO 2 :Al 2 O 3 molar ratio of at least 0.75:1 at a temperature in the range of from 1350°C to 1600°C. A process according to claim 7, wherein the mixture of mullite crystals and silica is formed by injecting an aluminosilicate material having a SiO 2 :Al 2 O 3 molar ratio of at least 0.75:1 and in finely-divided form, into a fluidized bed maintained at a temperature in the range of from 1000°C to 1800°C. A process according to claim 7, wherein the mixture of mullite crystals and silica is formed by injecting an aluminosilica material having a SiO 2 :Al 2 O 3 molar ratio of at least 0.75:1 and in finely divided form, into a vortex of hot gases maintained at a temperature in the range of from 1000°C to 1800°C. A process according to any one of claims 7 to 10, wherein the aluminosilicate material, before heat-treatment, is contacted with an aqueous solution containing transition metal cations. A process according to any one of claims 7 to 11, wherein the particulate product prepared in step (a) comprises particles substantially all of which have a size in the range of from 10 micrometres to 100 micrometres. A process according to any one of claims 7 to 12, wherein in step (b) the alkali metal hydroxide solution has a molarity of at least 3 M. A process according to any one of claims 7 to 13, wherein in step (b) the particulate product of step (a) is treated with the alkali metal hydroxide solution at a temperature in the range of from 80°C to the boiling point of the alkali metal hydroxide solution. A process according to any one of claims 7 to 14, wherein in step (c) the alkali-treated particulate product of step (b) is washed first with an alkaline solution weaker than that used in step (b) and then repeatedly with water until the washing medium is substantially free of silicate ions and alkali metal ions. A process according to any one of claims 7 to 15, wherein the particulate product of step (a) is prepared in the form of cellular bodies, each of which is a spherical hollow particle, by spray-drying an aqueous suspension of the aluminosilicate material. A process according to any one of claims 7 to 15, wherein the particulate product of step (a) is in the form of a cellular body prepared by foaming an aqueous suspension of the aluminosilicate material which is permitted to dry and set to a rigid foam comprising a plurality of internal particles. A packed column comprising the particulate porous material claimed in any one of claims 1 to 6. A filled plastics material wherein the filler comprises the particulate porous material claimed any one of claims 1 to 6. A filled natural or synthetic rubber composition wherein the filler comprises the particulate porous material claimed in any one of claims 1 to 6. A paper including a filler comprising a particulate porous material claimed in any one of claims 1 to 6.

Inventors: GOULD CARYL, JONES THOMAS RICHARD, GOULD, CARYL, JONES, THOMAS RICHARD
Applicants: ECC INT LTD, ECC INTERNATIONAL LIMITED
Application year: 1985
Main classification: B01J20
IPC codes: C01B33, B01J39, B01J47, B01J20, D21H17