CRYSTALLINE ENCILITE COMPOSITE, ITS PREPARATION AND USE

Abstract: A crystalline encilite catalyst composite for use in the conversion of alkanols to olefins, has the composition, on an oxide molar ratio basis: 1.0 ± 0.3 M₂O: Fe₂O₃: 30-300 SiO₂: ZH₂O where M is a monovalent cation and Z is an integer from 0 to 20, The catalyst composite is prepared by reacting, in an aqueous medium, iron, silicon, an alkali metal and, if desired, sulphuric acid with a tetraalkyl ammonium salt, heating the gel obtained, removing the supernatant liquid formed by such heating, recovering the solid residue, and washing, drying and calcining the latter.

Description: Crystalline encilite catalyst composite, its preparation and use The present invention relates to a novel crystalline ferrosilicate material, its production and use. More particularly, the invention relatea to the novel crystalline ferrosilicate referred to alternatively hereafter as "encilite" or "ferrosilicate encilite" zilch is active as a catalyst composite. The invention encompasses a process for the production of the novel ferrosilicate encilite catalyst composite and a method for the conversion of alkanols to olefins employing said encilite as catalyst. Prior art zeolites are exemplified best as crystalline aluminosilicates. These aluminosilicates possess a well ordered porous structure consisting of cavities which are interconnected by a number of channels. The dimensions of the channels and cavities are precisely defined and uniform. As a result, they accept for adsorption molecules of certain dimensions and reject molecules of larger dimension. This to the aforementioned ability of these materials to discriminate or 'sieve' various molecules depending on their dimensions, these material have also been known as 'molecular devesi A significant feature of the aluminosilicate zeolites is the catalytic activity exhibited by them in those reactions which are catalyeed by the presence of Bronsted acid sites. These zeolites possess a rigid framework of cross-linked B1O and AlO4 tetrahedra. The negative charge of the tetrahedra containing the trivalent aluminium ion is balanced bg the inclusion of a cation, usually an alkali metal ion, as a non-framework charge balancing ion. This non-framework alkyli metal cation can be replaced by conventional techniques of ion-exchange by other cations like NH4+, Ca2+, etc. The deammonisation of the zeolites containing the NH4+ cation yields the acid-form of the zeolite which is active in catalysing reactions like cracking, alkylation or isomerisation. One limitation of the zeolites of the prior art containing aluminium ions in lattice positions is that due to the hiih intrinsic acidic strength of the protons associated vith the aluminium, the catalytic selectivity of the zeolites in reactions which do not require such very strong acid sites, such as the conversion of methanol to a mixture of ethylene, propylene and butenes is lov and decreases with time-on-stream. In view of this drawback evinced by prior art zeolites when employed in catalytic reactions, efforts have been made to develop a solid zeolite-like material which, instead of aluminium ions, contains other cations in lattice position capable of imparting lover intrinsic acid strength te the associated protonic acid site and thereby increasing the selectivity and service life of the zeolite as a catalyst for the conversion of alkanols, snoh. as methanol, to light olefins. It is, therefore, a primary ob3ect of the present invention to provide an improved crystalline ferrosilicate material which replaces aluminium ions in lattice position by other cations in order both to increase the selectivity and enhanee the stability of the ferrosilicate as a catalyst in the conversion of alkanols to olefins. A more specific object of the invention lies in the provision of novel ferrosilicate encilite aluminium has been replaced by iron in the lattice position. Yet a further object of the invention resides in the synthesie of a novel encilite which when employed as catalyst in a catalytic reaction imparts a lower intrinsic acid strength to the associated pro tonic acid site. The invention also aims at a process for the preparation of such novel encilite which is active as a catalyst composite material. A still further object of the invention is a method employing such novel crystalline ferrosilicate encilite as a catalyst for the conversion of alkanols to light olefins. In its broadest aspect, the present invention provides a novel crystalline encilite catalyst composite having, in terms of oxide mole ratios, the following chemical composition: 1.0+0.3 X20 s Fe2O3 s 30-300 SiO2 : ZH20 wherein X is a monovalent cation and Z is a value from O to 20. According to a preferred feature, such novel ferrosilicate encilite of the invention has, in terms of oxide mole ratios, the following chemical composition: 1.0#0.2 M2O : Fe2O3 : 30-300 SiO2 : @H2O wherein Z and M have the meanings stated above. The present invention also provides a process for the preparation of a novel crystalline encilite catalyst composite said encilite having, in terms of oxide mole ratios, the following chemical composition: 1.0#0.3 M2O : Fe2O3 : 30-300 SiO2 : ZH2O wherein I is an monovalent cation and Z is a value from O to 20, which process comprises reacting in aqueous medium iron, silicon, an alkali metal and, if desired, sulphuric acid with a tetraalkyl ammonium salt of the formula: : RÚxRêyN+A wherein A is a bromide or hydroxide ion, RÚ and 22, which may be the same or different, are alkyl graups containing from 2 to 4 carbon atoms and x and y, which may We the same or different, are values between t and 3, the sum of the values of and y being equal to 4, heating the gel resulting from said reaction, removing supernatant liquor resulting from the heating, recovering the solid residue, washing the recovered solid, drying it and thereafter subjecting it to calcination. Preferably, the monovalent cation M in the composition of the ferrosilicate may be sodium, ammonium, hydrogen or a mixture of any of these. The ferrosilicate encilite resulting from the process may, according to a preferred feature of the invention, be treated further in order to improve its selectivity and stability as a catalyst composite by subjecting the calcined material to ion exchange with a salt of ammonia to obtain encilite having a molar ratio of sodium oxide to iron oxide in the range of from 0.05 to 0.3. In the specific embodiment when M is sodium, the ion-exchange to which the ferrosilicate encilite is 1BUb 8tmtially subjected is effective in replacing/the sodium ions in the encilite by NE4 ions. The product thus obtained is then further calcined in air, preferably at á temperature of about 400 C, to form a hydrogen ion solid composite. Preferably, the reaction to form the gel and provide the requisite cations for the synthesis of the encilite is effected by employing a tetraalkyl ammonium salt of the formula: RÚxRêyN+A wherein A is a bromide ion, R1 and Rê, which may be the same or different, are ethyl, propyl or butyl and x and y, which may be the same or different, are values between 1 and 3, the sum of the values of z and y being equal to 4. In accordance with a further feature of the invention, the aqueous reaction medium for formation of the gel has the following composition in terms of mole ratios: silicon (as silica) to 30 - 200 iron oxide sodium oxide to iron oxide 2 - 10 tetraalkyl ammonium salt 1 - 20 to iron oxide sulphuric acid to iron 1 - 5 oxide water to iron oxide 500 - 5000 By regulation of the quantity of iron in the synthesis medium, it is possible to vary the silicon to iron molar ratio in the final product in a range of from about 30 to about 300. Typical sources of iron which may be employed in the process of the present invention include the sulfates, nitrates, oxides and hydroxides of iron in various structural and textural forms. Examples of the sources of silicon employable in the inventive process include silicic acid and silicon oxides in various physical modifications such as colloidal silicon, fumed silica, chromatographic silica, silica gel and sodium silicate. Examples of the alkali metal cations which may be employed in the process of the invention include the hydroxides, nitrates and sulphates of alkali metals, Organic templates useful in process of this invention are tetraalkyl ammonium cations of the formulae RÚ Rê N Br or RÚ Rê NOH wherein RÚ, Rê, x and y have the x y x y meanings stated above. Preferred examples of such alkyl ammonium compounds include triethyl-n-propyl ammonium bromide, tetraprozyl ammonium bromide, and triethyl n-butyl ammonium bromide. it has been found that the presence in the reaction medium of alkyl ammonium ions of the type described along with alkali cations like Ha or K has a beneficial effect on the course of the nucleation and crystallisation of the desired encilite material. Moreover, it has been found that the absence of such ammonium ions in the reaction medium during crystallisation gave ris"e to a solid product which did not have a stable prolonged activity for the conversion of alkanols to hydrocarbons like light olefins. Preferably, the reaction to produce the gel is effected at a temperature in the range of from 100 C to 2OO0C over a period of from 1.to 15 days. Conveniently, the reaction'is carried out in an autoclave reactor under autogeneous pressure of steam in the above-mentioned temperature range. From the point of view of its physical capability to act as a molecular sieve, any zeolite is ascertained and evaluated in terms of its pore structure, i.e. the amount of water, a-hexPne, cyclohexane or 2-methylpentane that can be absorbed in the porous cavities of the material at 24 C. While the extent of hydrophilicity of the porous cavities is indicated by the amount of water adsorbed, the adsorption of n-hexane may be used to evaluate the hydrophobic nature of the internal source of the zeolite material as well as the total internal void volume of the said material. A comparison of the respective amounts of adsorption of n-hexane, neopentane, benzene and cyclohexane gives an indication of the diameter of the pores in the crystalline ferrosilicate since the three molecules mentioned hereinbefore differ mainly in their cross-sectional dimensions and otherwise possess a similar hydrophobic character. in order to assess the pore structures of the ferrosilicate of the present invention, an encilite sample was degassed at 400 C for 4 hours at a pressure lower than 10-8 bar. The sample was then cooled to 24 C. The sorbate was then admitted and the amount adsorbed at equilibrium was noted. It was invariably found that for the crystalline ferrosilicate prepared according to the present invention, the amount of n-hexane adsorbed per unit weight of solid was always higher than the amount of water adsorbed indicating thereby a highly hydrophobic nature of the internal surface within the pores of the encilite. The hydrophilicity, as measured by the amount of water adsorption and the surface acidity, as measured by the amount and strength of adsorption on the encilite, Was intermediate between the high values observed in the case of aluminosilicate zeolites and the very low values observed in the case of polymorphs of SiO2. The ferrosilicate encilite of this invention thus comprises a molecular sieve with an adsorption pore size near 610. At 240 C, it adsorbs molecules as large as benzene (kinetic diameter = 5.9A0) but rejects molecules larger than 6A such as neopentane (kinetic diameter = 6.2A0). In terms of its chemical structure, the encilite produced by the process of the present invention has a silica to iron oxide molar ratio of at least 30 but not more than .3, and a sodium oxide to iron oxide molar ratio of at least 0.7 but not more than 1.3. The iron ions in the encilite are in the trivalent positive oxidation state. This structure enables the encilite produced by the present invention to evince a number of advantageous characteristics which are discussed hereafter. First of all, there is the unique stability of its trivalent iron ions under conditions of ion-exchange. The reason for this lies in the fact that such trivalent iron ions Fe, are incorporated within the crystalline framework lattice of the enciliteitseif and are not simply present as non-framework cations in the intra-crystalline void volume where they could be easily replaced by other cations through conventional techniques of ion-exchange. Secondly, the trivalent iron ions present in the encilite of the present invention are uniquely stable against reduction. Once again, this is due to their incorporation within the crystalline framework lattice and their absence as non-framework cations in the intra-crystalline void volume where they could easily have been reduced to divalent or lower oxidation states (Be203 or Fe O ) and thence to metallic iron by conventional hydrogen reduction. The trivalent iron ions incorporated in the tetrahedral lattice framework of the encilite have been subjected to electron spin resonance spectroscopy. This shows them to evince a strong absorption band at g = 4.3 characteristic of Be3+ surrounded by four oxygen anions at the corners of a tetrahadron. This observation confirms that the trivalent iron ions in encilite are indeed present within the tetrahedral zeolitic lattice and ndt in nonframework positions, where they would have been surroundedby six oxygen amnions at the corners of an octahedron and hence would not exhibit the absorption band at g = 403 in the electron spin resonance spectrum. The encilite of this invention has an exceptionally high degree of thermal stability upto 1000 C, thereby rendering it especially suitable for use as a catalyst in processes involvin elevated temperatures. It would appear that the presence in the reaction mixture of both sodium and sited alkyl ammonium ions in addition to the oxides of silicon and iron is necessary to obtain solid encilite possessing the desired catalytic activity. Even though the precise mechanism by which alkyl ammonium ions, when present in the reaction medium, influence the rate and course of the crystallisation of the desired catalytic mass is not known in detail, it may be possible to speculate that they influence the structure of water in the vicinity of the reacting SiO4 and Fe tetrahedral species in such a way that nucleation and crystallisation occur leading to a product, i.e. encilite, which possesses both a desirable porous structure and which is active, selective and stable in the catalytic conversion of alkenols to olefins. Accordingly, the present invention further provides a method for the catalytic conversion of alkanols having from 1 to 4 carbon atoms, mixtures of alkanols or mixtures of such alkanols and water into hydrocarbons consisting essentially of light olefins which comprises contacting said alkanols or aqueous mixtures thereof at a temperature in the range of from 300 C to 500 C with a novel encilite catalyst composite having, in term of oxide mole ratios, the following chemical composition: 1.0#0.3 M2O : Fe2O3 : 30-300 SiO2 : ZH2O wherein M is a monovalent cation and Z is a value from O to 20. More particularly, X is sodium, ammonium, hydrogen t mixture of any of these. Preferably, the method involves contacting the alkanols or alkanol mixture in the vapour phase with said ferrosilicate encilite in the form of a hydrogen ion solid composite. According to a specific embodiment of the method in question, the encilite used is prepared by reaction in aqueous medium of iron, silicon, an alkali metal and, if desired, sulphuric acid with a tetraalkyl ammonium salt of the formula: R1 2 N+A x y wherein A is a bromide or hydroxide ion, RÚ and Rê, which may be the same or different, are alkyl groups containing from 2 to 4 carbon atoms and x and y, which may be the same or different, are values between 1 and 3, the sum of the values of x and y being equal to 4, followed by heating of the gel resulting from said reaction, recovery of the solid residue and calcination of the recovered solid. Conveniently, the ferrosilicate encilite catalyst is combined with a binder in order to impart greater mechanical strength thereto during its employment in the alkanol conversion. Examples of typical binders include silicon, alumina, bentonite, kaolinite or admixtures thereof. The ferrosilicate encilite is combined with such binder in an amount of from 50 to 95 by weight of catalyst based on the combined weight of catalyst and binder. When the binder is a clay-like material such as alumina, bentonite or kaolinite, a blend of catalyst and binder with water can be prepared to the desired consistency and the blend formed into a convenient shape, for instance by extrusion. The shape or extrudate is then dried before being employed in the method of conversion. The alkanol most suited for conversion by the method of the present invention is methanol but other alkanols having up to 4 carbon atoms can also be employed. In a specific embodiment of the method, the catalytic encilite is located within a downffow integral fixed bed reactor and vapours of methanol or other alkanol are passed over it at a weight hourly space velocity (WHSV) of 2 to 20. The structural features of the ferrosilicate encilite produced by the process of the present invention and employed in the alkanol conversion method described above can be ascertained by a variety of techniques. The findings listed in Table 1 hereafter were obtained by x-ray powder diffraction mesurements on a Philips PW 1730 diffractometer using copper K &alpha; -radiation in conjunction with a nickel filter. la such Table, the interplanar spacings are represented by '&alpha;' and are expressed in terms of Angstrom units (A) and the relative intensity values are represented by I/Io and are expressed in terms of the relative peak heights. The framework vibration frequencies (in cm-1) of encilite containing iron cations in lattice positions are shown in Table 2. The infrared spectra of encilite were recorded with a Perkin-Elmer infrared spectrometer. TABLE 1 X-RAY DIFFRACTION PATTERN OF ENCILITE-SODIUM FORM d I/Ig 11.0420 83.30 9*9945 62.57 TABLE 1 X-RAY DIFFRACTION PATTERN OF ENCILITE-SODIUN FORM d I/Ig 9.7096 15.90 7.4057 10.22 7.0752 6.93 6.6713 7.95 6.3203 11.36 5.9804 10.22 5.6755 9.19 5.5345 9.09 5.3679 3.40 5.1038 3.40 4.9087 5.68 4.5950 6.25 4.4357 3.40 4.3496 9.09 4.2467 15.99 4.0733 5.68 4.0080 9.09 3.8371 100.00 3.7416 34.09 3.7047 46.59 3.6449 31.81 3.4293 11.36 3.3285 5.50 3.2406 4.54 3.1291 2.84 3.0394 10.79 2.9378 5.60 TABLE 2 INFRARED FRAMEWORK VIBRATION FREQUENCIES FREQUENCY (CM-1) INTENSITY 455 MS 550 590 M 620 M 678 x 730 M 800 MS 870 MS 888 MS 1040 S 1100 s 1230 MS For appreciating the absorption at the intensity set out in Table 2, the following explanation is given: INTENSITY ABSORPTION (%) VW (very weak) Less than 10 W (weak) 10-19 M (medium) 20-39 MS (medium strong) 40-69 S (strong) 70-89 It should be understood that the x-ray diffraction and infrared framework vibration frequencies are characteristics of all species of encilite. Ion exchange of the sodium ions with other cations like H+, NH4+, K+, Ca2+ reveals aubstantially the same pattern with some minor shifts in interplanar spacings or vibration frequencies and variation in the relative intensity of the various peaks. Other minor variations can occur depending on the silicon to iron ratio of the particular sample as well as on the prolonged duration of its subjection to steam treatment at elevated temperatures. The invention in both its aspects will now be described in greater detail in the following Examples which describe non-limitatively the preparation of the novel encilite and its use in the conversion of alkanols to light hydro carbons. Where adsorption data are given, such data have been measured gravimetrically in a high vacuum adsorption system using a quartz spring balance. EXAMPLE This example illustrates the preparation of the ferrosilicate encilite. To 20 gms. of sodium silicate (8.2 x Na2O, 27.2 x 5i02, 26.9xH2O) 10 ml. of water were added to constitute solution A. 2.5 gins. of tetrapropyl ammonium bromide were dissolved in 10 ml. of water to yield solution B. 0.54 gms. of ferric sulphate (31.Z% Fe203) was added to water and heated to 500C to yield a clear solution C. 1.76 gms. of H2SO4(98x) were diluted in 15 m. of water to produce solution D. Solution B was added to solution A with stirring. Solution C was then added to the mixture with stirring. Finally, solution D was added to the resulting mixture dropwise with constant vigorous stirring. A solid gel was formed whose pH was about 10.2. The gel was heated at 180 C in a closed autoclave under autogeneous pressure of steam for 1 day. After this process, the autoclave was quenched in cold water. The autoclave was opened and the supernatant liquid separated from the solid product by filtration. The pH of the supernatant liquid was 11.8. The solid product was washed with hot water till the washings were free from sulphate ions. The solid was then dried in air in an oven at 120 C for 12 hrs. and calcined in air at 520 C for 8 hours to yield a solid crystalline material. The x-ray diffraction pattern of the material is set forth in Table 1. The infrared framework vibration frequencies of the material are given in Table 2. The chemical composition of the solid material was found to be 0.8 Na2O: Fe2O3: 71Si02. The electron spin resonance spectrum of this material was found to contain a sharp absorption band at g=4. 3. EXAMPLE 2 The procedure of Example 1 was repeated using triethyl-n-propyl ammonium bromide instead of tetrapropyl ammonium bromide. The solid material that was obtained exhibited an x-ray diffration pattern that was substantially the same as that set forth in Table 1. The framework vibration frequencies in the infrared region were also identical to that given in Table 2. The chemical composition of the solid material was found to be 0.92 Na2O: Fe2O3: 76Si02. EXAMPLE 3 This example illustrates the process for replacing the sodium ions in the crystalline ferrosilicate by ammonium ions. Samples oi the product of Example 1 were subjected to ion-exchange. The solid was treated twice with an aqueous solution of 5N ammonium chloride at 90 C for 15 hours each time. After each exchange, the product was washed with hot distilled water till the filtrate was free from chloride ions. The product thus obtained was dried at 1200C in air in an oven to yield the ammonium form of encilite. The molar ratio of sodium oxide to iron oxide in the material was 0.04. By varying the concentration of NH4Cl and the number of exchange , the sodium oxide ratios could be varied from 0.3 to 0.05. EXAMPLE 4 This sample illustrates the process for replacing the ammonium ions in the crystalline ferrosilicate by hydrogen ions. Samples of the product of Example 3 were calcined at 5200C for 10 hours in a stream of dry air to yield the hydrogen form of encilite. EXAMPLE 5 A silicate solution was made by mixing 500 g sodium silicate (27.2% Sio2, 8.4% Na2O and 63.9% R20), 87.2 g. dipropyl -diethyl bromide and 400 g of water. An acid solution was made by mixing 21.8 g. of ferric sulphate hexahydrate, 70.4 g H2S04 and 1600 g. of water. This acid solution was then added to the silicate solution slowly under vigorous stirring to form a firm gel. The pH of the gel was measured to be 10.2. The gel had the following composition in terms of mole ratios of oxides. 4.38 H2O: 25.5 Na2O : Fe2O3 : 83 SiO2 : 3365 H2O. where R is the dispropyl-diethyl cation. The resulting gel was charged into a one gallon autoclave. The crystallization was carried out at 150 C without agitation for 130 hours. The autoclave was quenched in water to cool it ro(fl temperature. The water-washed and dried 200 ,g. product was found to be a crystalline ferrosilicate characterized by x-ray diffraction (XRD) data as given in Table 1. EXAMPLE 6 The identical mixing sequence of Example 1 was followed and apart from a change in the cation of quarternary ammonium compound, the other reaction components were the same as Example 5. A gel was formed by mixing the following reaction components: i) 800 g. sodium silicate ii) 94.7 g. tripropyl-ethyl bromide + 400 g. 1120 iii) 70.4 g H2SO4 + 1200 g H2O. This gel had the following composition in terms of mole ratios of oxides: 4.38 R2O : 25.5 Na2O : Fe2O3 83 SiO2: 3365 H2O where R is s the tripropylethyl cation. The thick homogeneous gel mix was transferred to a one gallon autoclave and crystallized at 180 C without agitation for 48 hours. After quenching the autoclave to room temperature, the product was filtered, washed and dried. The product (200 g) exhibited a similar XRD pattern to that given in Table t, confirming it to be a crystalline ferrosilicate0 EXAMPLE 7 An encilite catalyst estrudate with increased mechanical strength was prepared by treating and mixing hydrogen forms of encilite ferrosilicate zeolite powder saturated with H20 vapour with bentonite clay at room temperature and shaping the mass by passing it through a screw driven steel-die with a 1/8 inch opening. The optimum content of bentonite was 15 per cent on dry basis. The extrudates were kept open to the atmosphere for 2 to 4 hours, dried in air in an oven at 100 C -1000C for about 4 hours and finally calcined in a muffle furnace at 550 C for 10 hours. EXAMPLE 8 In this example 1/8 inch extrudates of encilite catalyst were prepared by mixing hydrogen forms of encilite ferrosilicate zeolite powder with alumina binder at room temperature. The optimum content of alumina binder used was 50 per cent on dry basis. The encilite extrudates were dried in air in an oven at 100 C -110 C and then calcined in a muffle furnace at 550 0C for 10 hours before putting them to use. EXAMPLE 9 A solution was prepared by mixing 348.4 g of colloidal silicon dioxide (96.46% SiO2O. 3.77% H2O), and 609 ml tetrapropyl ammonium hydroxide (40% aqueous solution) in 200g of water. -The resulting mixture was stirred for 15 minutes. To this, a solution of 81.28g of ferric sulphate hexahydrate in 950 g. of water was added slowly under stirring. An alkali solution of 20.48 g. of sodium hydroxide in 675 g. of water was added to the prepared mixture slowly under stirring to form a homogeneous gel. The pH of the g measured to be 12.5. The gel had the following composition in terms of mole ratios of oxides: 3.75 R2O : 1.6 Na2O : Fe2O3: 35 SiO2: 425 H2O where R is the tetraalkyl ammonium ion. This gel was charged into a one gallon capacity stainless stell autoclave. The crystallization was carried out at 180 C without agitation for 140 hours. The autoclave was quenched in water and cooled to room temperature. The water-washed and dried product (340 g) was found to be a crystal- line ferrosilicate characterized by an x-ray diffraction pattern as shown in Table 1, EXAMPLE 10 In this example keeping the identical mixing sequence and procedure of Example 1, a gel was formed by mixing the following components: i) 560 g collodial silicon dioxide + 55 g H2O. ii) 153 ml. tetrapropylammonium (TPA) hydroxide (40% aq.) iii) 20.32 g Fe2 (SO4)3.6H2O + 75 g H2O iv) 5.12 g NaOH + 175 g H2O The gel so formed had the following composition in terms of mole ratios of oxides: 3,75 R2O : 1,6 Na2O : Fe2O3 : 225 SiO2 : 425 H2O where R is a tetrapropyl ammonium ion. The resulting homogenous gel was charged into a one gallon capacity stainless steel autoclave. The crystallization was carried out at 1800C without agitation for 140 hours. The autoclave was quenched in water and cooled to room temperature. The water-washed and dried product (550g) was found to be crystalline ferrosilicate characterized by XRD data as given in Table 1. EXAMPLE 11 In this example keeping the identical mixing sequence and procedure of Examples 1,and 2, a gel was formed by mixing the following components: i) 373 g. colloidal silicon dioxide + 160 g. 1120 ii) 305 ml. TPA-OR (40% aq. solution) iii) 40.64 g. Fe2(SO4)3 6H2O + 150 g. H2O iv) 10.24 g NaOH + 900 g H20 The gel formed had following composition in terms of mole ratios of oxides: 3.75 R2O : 1.6 Na2O s Fe2O3 : 75 SiO2 : 4251120 where R is a tetrapropyl ammonium ion. The resulting homogeneous gel mix was charged into a one gallon capacity stainless steel autoclave. The crystallization was carried out at 1800C without agitation for.140 hours. The washed and dried product (370 g.) was found to be a crystalline ferrosilicate characterized by XRD data given in Table 1. EXAMPLE 12 402 g chromatographic silica gel (90.2%) SiO2, 9.8% (H2O) were transferred to a stainless steel autoclave of one gallon capacity. A solution containing 169.3 g of tetra propyl ammonium bromide in 1000 g H2O was added to chromatrographic silica gel in the autoclave. To this slurry, 45.4 g sodium hydroxide in 1000 g water was then added with stirring to yield a homogeneous gel. An acid solution of 42.3 g ferric sulphate hexahydrate in 1387 g water was finally added slowly with vigorous stirring to form a gel mix. The stirring was continued for another 30 minutes to yield a homogeneous mix, the p11 of which was recorded to be 10.6. The gel has the following composition in terms of mole ratios of oxides. 3.82 R2O : 6.83 Na2O : Fe2O3 : 72.5 SiO2 : 2270 H2O: The autoclave was then closed and the crystallization was carried out at 180 C without agitation for 70 hours. The autoclave was quenched in water and cooled down to room temperature. The water-washed and dried product (400 g) was found to be a crystalline ferrosilicate characterized by XRD data as given in Table 1. EXAMPLE 13 In this example keeping the identical mixing sequence and procedure of Example 4, a gel mix was formed by mixing together the following components: i) 201 g chromatographic silica-gel ii) 169.3 g TPA¯Br + 1000 g H2O iii) 45.3 g NaOH + 1000 g H2O iv) 42.3 g Fe2(SO4)36H2O + 13@7 g. H2O The gel so formed had the following composition in terms of mole ratios of oxides: 3.82 R2O . 4.82 Na2O3 : Fe2O3 . 36 SiO2 : 1136 H2O where R is a tetraprppgl cation. The gel mix showed a 9H of 10.85. The gel was crystallized in an S.S. autoclave (1 gallon capacity) at 1800C without agitation for 90 hours. The autoclave was quenched as usual to cool it to room temperature. Tht water-washed and dried product (195 g) was found to be a crystalline ferrosilicate characterized by tRD data as given in Table 1. EXAMPLE 14 A silicate solution was made by mixing 800 g sodium silicate (27.2% SiO2, 8.4% Na2O, and 63.9% H2O), 84.2 g triethyl-n-propyl ammonium bromide and 400 g water. An acid solution was amde by mixing 21.8 g Fe2(SO4)3 6H2O, 70.4 g H2SO4 and 1600 g water. This acid solution was then added to the silicate solution under vigorous stirring to form a thick gel. The pH of the gel measured 10.5. The gel -had the following composition in terms of mole ratios of oxides: 4.38 R2O : 25.35 Na2O : Fe2O3 : 83 SiO2 : 3365 H2O where R is the triethyl-n-propyl cation. The resulting gel was charged into a one gallon capacity S.S. autoclave. The crystallization was carried out at 1800C without agitation for 49 hours. The autoclave was quenched as usual to cool it to room temperature. The water-washed and dried product (200 g.) was found to be a crystalline ferrosilicate characterised by gRD data as given in Table 1. The chemical composition of the hydrated product was analysed as Fe2 : 72 SiO2 : 0.8 Na20 : 10H2O. EXAMPLE 15 In this example, keeping the identical mixing sequence and procedure of Example 6, a gel was formed by mixing the following reaction components: i) 800 g sodium silicate ii) 84.2 g of triethyl-n-propyl ammonium bromide iii} 50.o g Fe2(SO4)3 6H20 + 500 g H20 iv) 56.08 g H2SO4 + 1000 g H2O The gel formed had the following composition in terms of mole ratios of oxides: 4.38 R2O : 25.35 Na2O : Fe2O3 : 36 SiO2 : 3365 H2O The resulting gel was charged into a one gallon S.S. autoclave and crystallized at 180 C without agitation for 96 hours. The product (200 was found to crystalline ferrosilicate. EXAMPLE 16 In another example, keeping the identical mixing sequence and procedure of Examples 6 and 7, a gel was formed by mixing the following reaction components: i) 800 g sodium silicate (27.2% SiO2, 8.4% Na2C) ii) 84.2 g of trientyl-propyl ammonim bromide + 500g H2O iii) 8.0 g Fe2(SO4)3 6H2O + 500 H2O iv)78.4 g H2SO4 + 1000 g H2O The gel formed had the following composition in terms of mole ratios of oxides: 4.38 R2O : 25.35 Na2O : Fe2O3 : 226 SiO2 : 3365 H2O The gel mix was crystallized at 1800C without agitation in a ene gallon S.S. autoclave for 30 hours. The autoclave was quenched and cooled down to room temperature as usual. The water-washed and dried product (200 g.) was found to 'be a crystalline ferrosilicate characterized by XRD data as given in Table 1. EXAMPLE 17 A silicate solution was made by mixing 800 g. sodium silicate (27.2% SiO2, 8.4% Na2O, and 63.9% H20), 100 g tetrapropyl ammonium bromide and 400 g of water. An acid solution was made by mixing 9.28 g of Fe(SO4)3 6H2O, 84 g H2SO4 and 1600 g of water. This acid solution was then added to the silicate solution slowly under vigorous stirring to form a thick gel. The pH of the gel was measured to be 10.5. The gel had the following composition in terms of mole ratios of oxides: 10 R2O : 58 Na2O : Fe2O3 : 194 SiO2 : 7492 H2. The resulting gel was charged into a one gallon capacity S. S. autoclave. The crystallization was carried out at 180 C, without agitation for 29 hours. The autoclave was quenched in water and cooled to room temperature. The waterwashed and dried product (200 g) was found to be a crystalline ferrosilicate characterized by an X-ray diffraction pattern as given in Table 1. EXAMPLE 18 In this Example keeping the identical mixing sequence and procedure of Example 9, a gel was formed by mixing together the following reaction compounds: i) 800 g sodium silicate ii) 100 g of tripropylammonium bromide + 400 g H20 i 12.4 g Fe2(SO4)3 61120 + 800 g 1120 iv) 73.6 g H2SO4 + 800 g H2O The gel so formed had the following composition in terms of more ratios of oxides: 7.75 NO : 44.7 Na2O : Fe2O3 : 150 SiO2 : 5576 H2O The resulting homogeneous gel was charged into a one gallon capacity S.S, autoclave. The crystallization was carried out at 1800C without agitation for 20 hours. The autoclave was quenched in water as usual. The water-washed and dried product (200 g) was found to be a crystalline ferrosilicate characterized by IRD data as given in Table 1. EXAMPLE 19 In this example keeping the identical mixing sequence and. procedure of Examples 9 and 10, a gel was formed by mixing the following reaction components: i) 800 g sodium silicate + 400 g 1120 ii) tOO g TPA-Br + 400 g H2O iii) 06.1-g Fe2(SiO4)3 6H2O + 400 g H2O The gel so formed had the following composition in terms of mole ratios of oxides: 15.61 H2O : 90 Na2O : Fe2O3 : 300 SiO2 : 11630 1120 The thick homogenous gel was transferred to a one gallon S.S. autoclave and crystallized at 1800C for 15 hours without agitation. After quenching the autoclave to room temperature as usual, the product was water-washed and dried. The product (200 g) exhibited an IRD pattern similar to that given in Table 1, confirming it to be a crystalline ferrosilicate. EXAMPLE 20 In this example, keeping the same sequence of mixing as the previous Examples, a gel was formed with the following reaction components: i) 800 g Sodium silicate + 900 g H20 ii) 100 g TPA-Br + 500 g H2O iii) 61.6 g Fe2(SO4)3 6H2O + 400 g H2O iv) 64 g H2SO4 + 800 g H2O The gel so formed had the following composition in terms of mole ratios of oxides: 1.56 R20 : 9 Na20 : Fe2O3 : 30 SiO2 : 1163 1120 The gel was charged into a one gallon S.S autoclave and crystallized at 180 C without agitation for 130 hours. The water-washed product after quenching the autoclave to room temperature was dried in air in an oven at 11000 for 4 hours. The product (200 g) was found to be a crystalline ferrosilicate characterized by XRD data as given in Table 1. EXAMPLE 21 In this example keeping the same SiO2/Fe2O3 ratio, i.e. 30, as in Example 20 with the same quantity of reactants except that the quantity of H SO was reduced to half, a gel 24 mix was formed. The pH of the. gel was measured to be 11.0. This gel was then crystallized as usual in a one gallon S.S autoclave at 1800C without agitation for 110 hours. The water-washed and dried product (200 g) was found to be a crystzlline ferrosilic ate. EXAMPLE 22 A solution was made by mixing 168 g collodial silicon dioxide (96.46 SiO2, and 3.72% H2O), 45 g terra propylammonium bromide and 400 g water. To this solution, 575 ml. liquor ammonia (25%NH3) and 15.48 g potassium hydroxide were added under stirring. An acid solution was made by mixing 7.48g Fe2(SO4)3 6H2O, 52.8 g H2SO4 and 1600 g of water. This acid solution was then added to the first solution slowly under vigorous stirring to form a thick gel. The gel had the following composition in terms of mole ratios of oxides: 9.66 H2O : Fe2O3 : 185 SiO2 : 287 (NH4)2O : 9.4 K2O 3292 H2O The resulting gel was charged into a one gallon S.S. autoclave. The crystallization was carried out at 150 0C without agitation for 150 hours. The autoclave was quenched in water and cooled to room temperature. The water-washed and dried product (4? g) was found to be a crystalline ferrosilicate with XRD data as given in Table 1. EXAMPLE 23 A silicate solution was made by mixing 600 g sodium silicate (27.2% SiO2, 8.4% Na2O and 63.9%H2O), 72.8 g tetrapropylammonium bromide and 400 g of water. To this, 575 ml, liquor ammonia (25% NH3) and 400 g of water were added slowly under stirring. An acid solution was made by mixing 7.48 g Fe2(SO4) 6H2O, 80 g H2SO4 and 1600 g water. This aid solution was then added slowly under vigorous stirring to iirst solution to form a homogenous gel. The gel had the following composition in terms of mole ratios of oxides: 9.8 R2O : 57 Na2O : Fe2O : 190 SiO2 (NH4)2O : 1092 H2O The resulting gel was charged into a one gallon S.S. autoclave and crystallized at 150 0C without agitation for 115 hours. The water-washed and dried product (150 g) was found to be a crystalline ferrosilicate. EXAMPLE 24 In this example, keeping the ssme SiO2/Fe2O3 i. e. 190, as in Example 23 with the same quantity of reactants but without liquor ammonia, a gel was formed. This gel was then crystallized as usual in a one gallon S.S. autoclave at 200 C without agitation for 16 hours. The water-washed and dried product (150 g) exhibited the similar XRD pattern as reported in Table 1. EXAMPLE 25 In this example 'keeping the same mixing sequence and procedure as in Examples 9, 10 and 11, a gel was formed by combining the following reaction components: i) 800 g sodium silicate ii) 100 g TPA-Br + 400 g H2O iii) 21-6 g Fe2(S04)3 6H20 + 400 g H20 iv) 70.4 g 112504 + 1200 g 1120 The gel so formed had the following composition in terms of mole ratios of oxides: 4.43 R2O : 25.5 Na20 . Fe2O3 : 85 SiO2 : 3292 H2O The gel mix was crystallized as usual in a one gallon S.s. autoclave at 2000C without agitation for 16 hours. The product (200 g)exhibited the similar XR9 pattern as given in Table 1, confirming it to be a crystalline ferrosilicate. EXAMPLE 26 In this example, the same molar ratio of SiO Fe2O3 as previous Examples and other conditions were maintained unchanged except that crystallization was carried out at 1800C without agitation for 48 hours. The product (200 g.) exhibited the similar nW pattern as given in Table 1, confirming it to be a crystalline ferrosilicate. EXAMPLE 27 In this example, the same sequence of mixing and the same composition of the gel in terms of mole ratios of oxides as in example 21 was maintained except that the gel was crystallized at 16000 without agitation for 72 hours. The product (200 g) wae found to be a crystalline ferrosilicate. The chemical composition of the water-washed, dried and activated sample was analyzed to be: SiO2 : 92.1% wt. Fe2O3 : 3.31% wt. Na2O : 1.06% wt. H2O : 3.443% wt. EXAMPLE 28 In this, example the parameters, reactants and molar ratios of Examples 18 and 19 were maintained except that the crystallization was carried out at 14000 without agitation for 96 hours. The product (200 g) wasfound to be a crystalline ferrosilicate conforming the XRD data as given in Table 1. EXAMPLE 29 A silicate solution was made by mixing 800 g sodium silicate (27.2% SiO2, 8.4% Na2O and 63.9% H2O), 100 g of tetra propylammonium bromide and 400 g water. An acid solution was made by mixing 21.72 g Fe2(SO4)3 6H2O, 70.4 g of H2SO4 and 1600 g of water This acid solution was then added to the silicate solution slowly under vigorous stirring to yield a thick gel. The pE of the gel was measured to be 10.25. The gel had the following composition in terms of mole ratios of oxides: 4.42 R2O : 25.5 Na2O : Fe2O3 : 86 SiO2 : 3292 H2O where R is tetrapropylammonium ion. The resulting gel was charged into a one gallon S.S. autoclave and crystallized at 180 C without agitation for 48 hours. The autoclave was quenched in water and cooled to room temperature. The water-washed, dried and activated (at 5500C for 10 hours) product (200 g) was found to be a crystalline ferrosilicate characterized by an X-ray diffraction pattern as shown in Table 1. The adsorption properties of the activated form of encilite are as follows: ADSORBATE TEMPERATURE P/P g/100 g. Cyclohexane 240C 0.84 3.84 n-hexane -do- 0.83 10.94 water -do- 0.78 7.97 EXAMPLE 30 A solution was made by mixing 200 g sodium silicate (27.2% SiO2, 8.4% a2O and 63.9% H20), 49.9 g tripropylamine and 42.1 g n- propyl bromide in 200 g of water. The resulting mixture was stirred for 15 minutes. To this, an acid solution of 20.32 g ferric sulphate hexahydrate and 86.8 g 112504 in 1800 g of water, was added slowly under vigorous stirring to form immediately a firm gel. This gel was then stirred for another 30 minutes to yield a homogenous mixture. The pR of the gel was measured to be 9.4. The gel had the following composition in terms of mole ratios of oxides: 4.29 R2O : 27.4 Na2O : Fe2O3 : 88SiO2 : 3505 H2O. The homogenous gel thus formed was charged into a one gallon S.S. autoclave and crystallized at 180 C without agitation for 8 days. The autoclave was quenched in water and cooled to room temperature. The water-washed and dried product was found to be a crystalline ferrosilicate characterized by ZRn data as given in Table 1. EXAMPLE 31 To examplify a preferred embodiment of this invention, a silicate solution was prepared in a 600 ml. capacity S.S. autoclave by mixing t20 gms. of sodium silicate, t3.44 s of trietbyl n-butyl nmmonlum bromide and 150 gms of water. An acid solution prepared by mixing 3.26 gms of ferric sulphate hexahydrate, 10.56 gas of sulfuric acid and 150 gms of water was added slowly kto the silicate solution under vigorous stirring to form a homogenous gel. The p/E of the gel was 10.0 # .2. The autoclave was closed and crystalization was carried out at 180 C while stirring the mixture at 100 RPM for 96 hours. The autoclave was quenched to room temperature. The pH of the supernatant liquid was 11.6 # 0.2. The solid product was filtered out from the liquid, water washed and dried at 100 -110 C in air in an oven for 10 hours. The dried product was calcined at 5500C for 4 hours. The product obtained after calcination was encilite with characteristic XRD pattern as given in Table 1. This was converted to the acid form by the procedure given in Examples 3 and 4. The hydrogen form of encilite thus obtained was mixed with 20% bentonite and 15% kaolinite on dry basis and formed into extrudates by the procedure given in Example 7. EXAMPLE 32 Methanol was passed in the vapour phase at atmospheric pressure over aa encilite catalyst, the catalyst being located in a downflow integral fixed bed reactor. The vapour was passed at a weight hourly space of 5.1, and in this connection, it is clarified that WHSV is the weight in gramS of the reactant, in this case methanol, which is passed over 1 gm. of the catalyst per hour at the specified temperatures and pressures mentioned hereunder. The products of the reaction were analysed quantitatively by gas chromatography. The results are illustrated in Table 3 hereafter. TABLE 3 CONVERSION OF METHANOL TO HYDROCARBONS Feed 100% methanol WHSV (hr-1) 2.2 Pressure Atmospheric Temp. 450 C Conv. of methanol 100% PRODUCT DISTRIBUTION (Wt.Z) Dimethyl ether Ril PARAFFINS C1 2.7 C2 Trace C3 5.1 C4 7.8 OLEFINS C2 10.3 C3 21.6 15.5 and other aliphatics AROMATICS Benzese 0.7 Toluene 3.2 Xylene 7.4 C9+C10 5.0 EXAMPLE 33 The effect of temperature on the conversion of methanol to hydrocarbons is illustrated in this example. The experiment and the analysis of the products obtained were carried out as in Example 32. The results are tabulated in Table 4. TABLE 4 CONVERSION OF METHANOL TO HYDROCARBONS: EFFECT OF TEMPERATURE Feed 100% methanol WHSV (hr-1) 2.2 Pressure Atmospheric Temp. C 300 365 405 450 500 % conv. methanol 54.4 83.6 99 100 100 PRODUCT DISTRIBUTION (Wt.%) 92.5 7.4 1.1 0 0 Dimethyl ether Paraffins C1 0.2 0.5 0.4 2.7 1.7 C2 TRACES C3 Trace 3.2 4.1 5.1 3.8 C4 0.2 11.9 14.1 7.7 6.7 OLEFINS 2 2.0 8.5 5.2 10.3 11.1 C3 2.1 8.4 10.7 21.6 19.2 4 1.4 10.8 12.1 15.5 15.1 + aliphatics 1.5 56.6 53.3 37.0 42.3 and aromatics 2 to e olefins 5.5 27.7 28.0 47.4 45.4 EXAMPLE 34 This example illustrates the effect of space velocity on the methanol conversion to hydrocarbons. Table 5 hereafter indicates the results of this effect. The experimental and analytical procedures were similar to those of Example 32. TABLE: 5 CONVERSION OF METHANOL TO HYDROCARBONS EFFECT OF SPACE VELOCITY Feed 28.5% methanol Pressure Atmospheric Temperature 4500C WHSV (hr.-1) 2.1 4.4 5.9 8.8 11.7 17.6 % conv. methanol 100 100 100 100 94.7 89.9 PRODUCT DISTRIBUTION (Wt.%) Dimethyl ether A A A A 0.4 0.9 Paraffins C1 2.4 1.9 1.3 3.1 2.2 2.8 C2 TRACES C3 3.5 0.9 0.7 0.6 0.7 0.4 C4 5.7 1.8 2.1 2.2 2.3 1.4 OLEFINS C2 11.6 9.4 7.8 8.9 8.0 9.1 C3 25.9 43.7 42.9 39.8 41.1 41.3 C4 18.8 20.5 21.21 16.1 17.4 15.6 C5+aliphatic + aromatics 32.2 21.8 23.9 29.5 28.3 29.5 C2 to C4 56.2 73.6 71.8 64.7 66.5 65.9 Olefins EXAMPLE 35 The concentration of methanol in the feed greatly influences the formation of olefins in the conversion of methanol to hydrocarbons. This is illustrated in this example and the results are tabulated in Table 6 herein. The methanol conversion and the analysis of the products were carried out as in Example 32 TABLE 6 CONVERSION OF METHANOL TO HYDROCARBONS EFFECT OF CONCENTRATION OF METHANOL IN THE FEED HS WHSV (hr-1) 4.4 Pressure Atmospheric Temp. 4500C Methanol concentration in the feed (% methanol in water v/v) tOO 71 44.3 28.5 % conv. of methanol 100 100 tOO 100 Product distri bution (Wt.%) Dimethyl ether A A A A Paraffins C1 2.7 2.5 1.7 1.9 C2 TRACES C3 5.1 3.5 1.4 0.9 C4 7.7 5.7 2.9 1.8 Olefins C2 10.3 11.7 9.4 9.4 C3 21.6 25.9 37.6 43.7 C4 15.5 18.7 23.7 21.0 C5+aliphatics + aromatics 37.0 32.2 23.3 21.8 C2 to C4 olefins 47.4 56.2 70.8 73.7 EXAMPLE 36 The aging effect of encilite with time-on-stream of the feed during the conversion of methanol to hydrocarbons is given in this example. The experimental procedures and the analysis of the products were carried out as illustrated in Example 32 The results are given in Table 7 hereafter. TABLE 7 CONVERSION OF METHANOL TO HYDROCARBONS EFFECT OF TIME ON STREAM OF THE FEED Catalyst Weight 3.2 gms WHSV (hr-1) 4.4 Temperature 450 C Feed 28.5% methanol 9 (v/v) Cumulative feed 350 980 1140 1350 1550 in ml. Product distribution (Wt.%) Dimethyl ether A A A A A Paraffins C1 1.9 1.9 1.4 1.5 1.7 C2 TRACES C3 o.g 0.9 0.8 0.9 0.9 C4 1.8 1.6 2.0 1.7 3.6 Olefins C2 9.4 9.7 8.4 8.0 9.7 C3 43.7 45.6 44.5 41.6 45.3 C4 20.6 20.0 21.0 17.2 17.0 C5+aliphatics +aromatics 21.8 20.4 21.9 30.0 21.2 C2 to C4 olefins 73.6 73.2 73.8 66.8 72.0 EXAMPLE 37 This example illustrates the product distribution obtained when using aqueous methanol at a reaction temperature of 500 C The methanol conversion and the analysis of the products are carried out as in Example 32. TABLE 8 CONVERSION OF METHANOL Methanol concentration in the feed (% methanol in water V/V) 71 Pressure Atmospheric Temperature Orr 0 500 WHSV 2.2 4.4 % Conversion of methanol 100 100 PRODUCT DISTRIBUTION (% Wt.) Dimethyl ether 0 0 Paraffins 5.5 5.8 C2 A A C3 2.9 1.8 4 3.1 1.8 Olefins 2 14.7 16.0 C3 27.4 30.5 C4 18.4 15.8 C5+hydrocarbons 28.1 28.3 C2 to C4 olefins 60.5 62.3 EXAMPLE 38 This example illustrates the product distribution obtained when using ethyl, propyl and butyl alcohols as the feedstock. The alkyl alcohol conversion and the analysis of the products are carried out as in Example 32. TABLE 9 CONVERSION OF ALKYL ALCOHOLS Temperature 450 C Pressure Atmospheric WHSV (hr.-1) 2.2 Feed Pure (100%) alcohol Alcohol ethanol propanol butanol Conversion of 100 100 100 alcohol (%) Product distribution (Wt.%) Paraffins C1 2.5 3.1 2.1 C2 0.7 0.4 0.8 C3 .4.5 3.8 5.1 C4 8.9 7.7 9.0 Ol efins C2 18.5 14.1 12.5 C3 20.2 23.8 21.8 C4 17.0 19.5 21.2 C5+aliphatics 20.4 18.0 10.5 aromatics 7.3 9.7 16.9

Claims: CLAIMS: 1. Crystalline encilite catalyst composite having, in terms of oxide mole ratios, the following composition: 1.0 # 0.3 M2O : Fe2O3 : 30-300 SiO2 : ZH2O wherein I is a' monovalent cation and % is a value from 0 to 20. 2. Crystalline encilite catalyst composite having, in terms of oxide mole ratios, the following composition: %1.0 # 0.2 M2O . Fe2O3 . 30-300 SiO2 : ZH2O wherein I is a monovalent cation and Z is a valve from o to 20. 3. Crystalline ferrosilicate as claimed in claim 1 or 2, wherein M is sodium, ammonium, hydrogen or a mixtuire of any of these. 4. Process for the preparation of a novel crystalline encilite catalyst composite having, in terms of oxide mole ratios, the following composition: 1.0 # 0.3 M2O : Fe2O3 : 30-300 SiO2 : ZH2O wherein M is a monovalent cation and Z is a value from 9 to 20, which process comprises reacting in aqueous medium iron, silicon, an alkali metal and, if desired, sulphuric acid with a tetraalkyl ammonium salt of the formula: : R1xR2yN+A wherein A is a bromide or hydroxide ion, R1 and R2, which may be the same or different, are, alkyl groups containing from 2 to 4 carbon atoms and x and y, which may be the same or different, are values between 1 and 3, the sum of the values of x and y being equal to 4, heating the gel resulting from said reaction, removing supernatant liquor resulting from the heating, recovering the solid residue, washing the recovered solid, drying it and thereafter subjecting it to calcination. 5. Process as claimed in claim 4, wherein N is sodium, ammonium, hydrogen or a combination of any of these. 6. Process as claimed in claim 5, wherein the calcined ferrosilicate encilite is subjected to ion exchange with a salt of ammonium to obtain encilite having a molar ratio of sodium oxide to iron oxide in the range of from 0.05 to 0.3. 7. Process as claimed in claim 5, wherein, when N is sodium, the calcined ferrosilicate encilite is subjected to ion exchange in order to replace substantially the sodium ions thereof by NH4 ions, the product thus obtained being further calcined in air to provide a hydrogen ion solid composite. 8. Process as claimed in any of claims 4 to 7, wherein in the tetraalkyl ammonium salt of the formula: 1 2P+ A is a bromide ion and R1 and R2 are ethyl, propyl or butyl. 9. Process as claimed in any of claims 4 to 8, wherein the aqueous reaction medium for formation of the gel has, in terms of mole ratios, the following co silicon (as silica) to 30 - AOu iron oxide sodium oxide to iron oxide 2 - RO tetraalkyl ammonium salt 1 - 20 to iron oxide sulphuric acid to iron t - 5 oxide water to iron oxide 500 - 5000. 10. Process as claimed in any of claims 4 to 9, wherein the silicon content of said aqueous medium is selected from silicic acid and silicon oxides such as colloidal silicon, fumed silica, chromatographic silica, silica gel and sodium silica. 11. Process as claimed in any of claims 4 to 10, wherein said tetrasikyl ammonium salt is selected from triethyl-n-propyl ammonium bromide, tetrapropyl ammonium bromide and triethyl n-butyl ammonium bromide. 12. Process as claimed in any of claims 4 to 11, wherein the sulphuric acid of the aqueous reaction medinni is formed in situ. 13. Process as claimed in any of claims 4 to 12, wherein said gel-forming reaction is effected at a temperature in the range of from 1000C to 2000C over Åa period of from I to 15 days. 14. Process as claimed in any of claims 4 to 13, wherein said calcination is effected at a temperature above 400 C. 15 Process for the preparation of a novel crystalline encilite catalyst composite, substantially as herein described in any one of foregoing Examples 1 to 31. 16. Crystalline encilite catalyst composite whenever prepared by the process claimed in any of clainLS 4 to 15. 17. Method for the catalytic conversion of alkanols having from t to 4 carbon atoms, mixtures of alkanols or mixtures of such alkanols and water into hydrocarbons consisting eseentially of light olefins which comprises contacting said alkanols or aqueous mixtures thereof at a temperature in the range of from 3000C to 5000C with a novel encilite catalyst oomposite having, in terms of oxide mole ratios, the following composition: 1.0 # 0.3 M2O : Fe2O3 : 30-300 SiO2 : ZH2O wherein M is a monovalent cation and Z is a value from o to 20. 18. Method as claimed in claim 17, wherein M is sodium, ammonium, hydrogen or a combination of any of these. 19. Method as claimed in claim 1 or 2, wherein said encilite catalyst composite is prepared from the reaction in aqueous medium of iron, silicon, an alkali petal and, if desired, sulphuric acid with a tetraalkyl ammonium salt of the formula: R1 R2 N+A x y wherein A is a bromide or hydroxide ion, R1 and 22, which may be the same or different, are alkyl groups containing from 2 to 4 carbon atoms and x and y, which may be the same or different, are values between 1 and 3, the sum of the values of x and y being equal to 4, followed by heating of the gel resulting from said reaction, recovery of the solid residue and calcination of the recovered solid. 20. method as claimed in any of claims 17 @@ @@@ wherein said alkanols or alkanol mixtures are contacted in the vapor phase with said ferrosilicate encilite in the form of a hydrogen ion solid composite. 21. Method as claimed in any of claims 17 to 20, wherein said ferrosilicate encilite catalyst in an amount of fron 50% to 95% by weight is combined with a binder in order to impart to the catalyst greater mechanical strength. 22. Method as claimed in claim 21, wherein said binder is selected from silicon, alumina, bentonite, kaolinite or admixturers thereof. 23. Nethod as claimed in claim 22, wherein said ferrosilicate encilite catalyst and one or more of said alumina, bentonite or kaolinite are blended with water to the desired Consistency and formed into any convenient shape, said shape being dried before being employed as the catalyst in the conversion method. 24. Method as claimed in any of claims 17 to 23, herein the mixture of alkanols and water contains from 28* to 71% by volume alkanol. 25. Method as claimed in any of claims 17 to 24, wherein the ferrosilicate encilite catalyst is located within a downflow integral fixed bed reactor and vapours of alkanol are passed over it at a weight hourly space velocity (WHSV) of 2 to 20. 26. Method as claimed in any of claims 17 to 25, wherein the alkanol is methanol. 27. Method for the catalytic conversion of alkanols having from I to 4 carbon atoms, mixtures of alkanols or mixtures of such alkanole and water into hydrocarbon consisting essentially of light olefins which comprise contacting said alkanols or aqueous mixtures thereof at a temperature in the range of from 30000 to 5000C with a novel crystalline encilite catalyst composite as claimed in claim 16. 28. Nethod for the catalytic conversion of alkanols into hydrocarbons consisting essentially of light olefins, substantially as herein described in any of foregoing Examples 32 to 38. 29. Light olefinic hydrocarbons whenever prepared by the method claimed in any of claims 17 to 28.

Inventors: BALAKRISHNAN, IKKANDATH, BORADE, RAMESH BABASAHEB, HEDGE, SURYAKANT GANESH, KULKARNI, SUNEETA BALVANT, RAO, BOLLAPRAGADA SESHAGIRI, RATNASAMY, PAUL
Applicants: COUNCIL OF SCIENTIFIC AND INDUSTRIAL RESEARCH
Application year: 1984
Main classification: B01J29
IPC codes: B01J29, C07C9, C07C15, C07C1