CRYSTALLINE SILICOPHOSPHOALUMINATE

Abstract: A new crystalline silicophosphoaluminate designated MCM-9 and having a particular crystal structure is provided. This crystalline material has ion-exchange properties and is readily convertible to catalytically active material.

Description: CRYSTALLINE SI LICOPEOSPHOALUMINATE This invention relates to a novel synthetic crystalline silicophosphoaluminate molecular sieve material, hereinafter 'NCM-9", containing aluminum, silicon and phosphorus in its framework, to a method for its synthesis and to use thereof in catalytic conversion of organic compounds. The crystalline material of this invention exhibits ion-exchange properties and can easily be converted to catalytically active material. Zeolitic materials, both natural and synthetic, have been demonstrated in the past to have catalytic properties for various types of hydrocarbon conversion. Certain zeolitic materials are ordered, porous crystalline aluminosilicates having a definite crystalline structure as determined by X-ray diffraction, within which there are a large number of smaller cavities which may be interconnected by a number of still smaller channels or pores. These cavities and pores are uniform in size within a specific zeolitic material. Since the dimensions of these pores are such as to accept for adsorption molecules of certain dimensions while rejecting those of larger dimensions, these materials have come to be known as "molecular sieves" and are utilized in a variety of ways to take advantage of these properties. Such molecular sieves, both natural and synthetic, include a wide variety of positive ion-containing crystalline aluminosilicates. These aluminosilicates can be described as rigid three-dimensional frameworks of SiO4 and Al O4 in which the tetrahedra are cross-linked by the sharing of oxygen atoms whereby the ratio of the total aluminum and silicon atoms to oxygen atoms is 1:2. The electrovalence of the tetrahedra containing aluminum is balanced by the inclusion in the crystal of a cation, for example an alkali metal or an alkaline earth metal cation. This can be expressed wherein the ratio of aluminum to the number of various cations, such as Ca/2, Sr/2, Na, K or Li, is equal to unity. One type of cation may be exchanged either entirely or partially with another type of cation utilizing ion exchange techniques in a conventional manner. By means of such cation exchange, it has been possible to vary the properties of a given aluminosilicate by suitable selection of the cation. The spaces between the tetrahedra are occupied by molecules of water prior to dehydration. Prior art techniques have resulted in the formation of a great variety of synthetic zeolites. The zeolites have come to be designated by letter or other convenient symbols, as illustrated by zeolite A (U.S. Patent 2,882,243), zeolite X (U.S. Patent 2,882,244), zeolite Y (U.S. Patent 3,130,007), zeolite ZK-5 (U.S. Patent 3,247,195), zeolite ZK-4 (U.S. Patent 3,314,752), zeolite ZSM-5 (U.S. Patent 3,702,886), zeolite ZSM-ll (U.S. Patent 3,709,979), zeolite ZSM-12 (U.S. Patent 3,832,449), zeolite ZSM-20 (U.S. Patent 3,972,983), zeolite ZSM-35 (U.S. Patent 4,016,245), zeolite ZSM-38 (U.S. Patent 4,046,859), and zeolite ZSM-23 (U.S. Patent 4,076,842) merely to name a few. The crystalline silicophosphoaluminate of the present invention is not an aluminosilicate zeolite, but it is a molecular sieve material with an ordered pore structure which accepts cert- .I molecules while rejecting others. Aluminum phosphates are taught in U.S. Patents 4,310,440 and 4,385,994, for example. Aluminum phosphate materials have electroneutral lattices and, therefore, are not useful as ion-exchangers or as catalyst components. U.S. Patent 3,801,704 teaches an aluminum phosphate treated in a certain way to impart acidity. The phosphorus-substituted zeolites of Canadian Patents 911,416; 911,417 and 911,418 are referred to as "aluminosilicophosphate" zeolites. Some of the phosphorus therein appears to be occluded, not structural. U.S. Patent 4,363,748 describes a combination of silica and aluminum-calcium-cerium phosphate as a low acid activity catalyst for oxidative dehydrogenation. Great Britain Patent 2,068,253 discloses a combination of silica and aluminum-calcium-tungsten phosphate as a low acid activity catalyst for oxidative dehydrogenation. U.S. Patent 4,228,036 teaches an alumina-aluminum phosphate-silica matrix as an amorphous body to be mixed with zeolite for use as cracking catalyst. U.S. Patent 3,213,035 teaches improving hardness of aluminosilicate catalysts by treatment with phosphoric acid. The catalysts are amorphous. U.S. Patent 2,876,266 describes an active silicophosphoric acid or salt phase of an amorphous material prepared by absorption of phosphoric acid by premolded silicates or aluminosilicates. Aluminum phosphates are well known in the art as exampled by U.S. Patents 4,365,095; 4,361,705; 4,222,896; 4,210,560; 4,179,358; 4,158,621; 4,071,471; 4,014,945; 3,904,550 and 3,697,550. Since their neutral framework structure is void of ion-exchange properties, they are used as catalyst supports or matrices. The crystalline silicophosphoaluminate synthesized hereby is a molecular sieve framework exhibiting ion-exchange properties and is easily and conveniently converted to material having intrinsic catalytic activity. The present invention is directed to a novel synthetic crystalline silicophosphoaluminate molecular sieve material, hereinafter designated 'WX)M-9t', containing aluminum, silicon and phosphorus and to its use as a catalyst component in catalytic conversion of organic, e.g hydrocarbon, compounds. The anhydrous crystalline MCTI-9 has the general formula: m+ n Mxm/m:(A1O2)-1-y:(PO2)+1-x:(SiO2)x+y:Ny/n wherein M is a cation of valence m, N is an anion of valence n, and x and y are numbers of from greater than -1 to less than +1 which satisfy the relationships: (1) if x is 0, then y is not 0, (2) if y is 0, then x is not 0, and (3) x + y is greater than 0.001 and less than 1. In the composition above, when x is greater than y, the silicophosphoaluminate is a cation exchanger with potential use as an acidic catalyst. When x is less than y, the silicophosphoaluminate is an anion exchanger with potential use as a basic catalyst. Such MCM-9 crystalline material has the characteristic X-ray diffraction pattern, in its calcined form, as set forth in Table 1-B hereinafter. In the as-synthesized form of the MLM-9, the silicophosphoaluminate can also contain occluded organic material, A, and water molecules, entrapped during the synthesis and filling the microporous voids. It then has the general formula: m+ n vA:M###:(A1O2-)1-y:(PO2)+1-x:(SiO2)x+y:N###:w(H2O) wherein v is the number of moles of A, occluded organic material resulting from organic directing agent and/or water immiscible organic solvent used in synthesis of and filling microporous voids of the MCM-9, which material may be removed upon calcination, w is moles of H20, e.g. from 0 to 5, and x and y are the numbers defined above. The f2M-9 crystalline material in the as-synthesized form has the characteristic X-ray diffraction pattern as set forth in Table 1-A hereinafter. The crystalline silicophosphoaluminate of this invention is a unique composition of matter which exhibits a valuable combination of catalytic, sorption and ion-exchange properties which distinguishes it from known aluminum phosphates. The silicophosphoaluminate material of the present invention will exhibit unique and useful catalytic, sorptive and shape selective properties along with a silicon/(aluminum + phosphorus) atomic ratio of less than unity, but greater than zero, e.g., from 0.001 to 0.99. It is well recognized that aluminum phosphates exhibit a phosphorus/ aluminum atomic ratio of only 0.8 to 1.2 and contain no silicon. Also, the phosphorus-substituted zeolite compositions, sometimes referred to as "aluminosilicophosphate zeolites", have a silicon/aluminum atomic ratio of from 0.66 to 8.0, and a phosphorus/aluminum atomic ratio of from greater than 0 to 1.0. The original cations of the as synthesized MCM-9 can be replaced in accordance with techniques well known in the art, at least in part, by ion exchange with other cations. Preferred replacing cations include metal ions, hydrogen ions, hydrogen precursor, e.g., ammonium, ions and mixtures thereof. Particularly preferred cations are those which render the MCM-9 catalytically active, especially for hydrocarbon conversion. These include hydrogen, rare earth metal and metals of Groups IA, IIA, IIIA, IVA, IB, IIB, IIIB, IVB and VIII of the Periodic Table of the Elements. Typical ion exchange technique would be to contact the synthetic MCM-9 with a salt of the desired replacing cation or cations. Examples of such salts include the halides, e.g. chlorides, nitrates and sulfates. The framework topology of the MCM-9 containing silicon, phosphorus and aluminum in tetrahedrally coordinated structural positions is similar to a synthetic aluminum phosphate described in U.S. Patent 4,310,440. The crystalline MCM-9 of the present invention can be beneficially thermally treated, either before or after ion exchange. This thermal treatment is performed by heating the silicophosphoaluminate in an atmosphere such as air, nitrogen, hydrogen, steam, etc., at a temperature of from 3000C to 11000C, preferably from 3500C to 750 C, for from 1 minute to 20 hours. While subatmospheric or superatmospheric pressures may be used for this thermal treatment, atmospheric pressure is desired for reasons of convenience. MCM-9 exhibits a definite X-ray diffraction pattern which distinguishes it from other crystalline materials. The X-ray diffraction pattern of the as synthesized MCM-9 has the following characteristic values: Table 1-A Interplanar d-Spacing (A) Relative Intensity 16.41 + 0.1 vs 10.84 + 0.1 w 9.33 +-0.1 w 8.20 + 0.1 m 6.68 + 0.05 w 6.17 + 0.05 w 5.65 + 0.05 w 5.46 + 0.05 w 4.74 + 0.05 w 4.34 + 0.05 w 4.21 + 0.05 5 4.10 + 0.03 m 4.05 + 0.03 m 4.00 + 0.03 w 3.94 + 0.03 m 3.83 + 0.03 m 3.77 + 0.03 w 3.64 + 0.03 w 3.59 + 0.02 w 3.39 + 0.02 w 3.28 + 0.02 m 3.16 + 0.02 w 3.09 + 0.02 w 3.03 + 0.02 w 2.95 <RTI ID=6.13> + 0.02 w 2.90 + 0.02 w 2.74 + 0.02 w 2.63 + 0.02 w Table 1-B list the characteristic diffraction lines of the calcined (4500C, atmospheric pressure, 4 hours) form of ?ICM-9. Table 1-B Interplanar d-Spacing (A) Relative Intensity 16.36 + 0.10 m 14.05 + 0.10 w 10.92 + 0.10 w 8.94 + 0.10 m 8.19 T 0.10 w 6.90 + 0.05 w 5.50 + 0.05 m 4.47 + 0.05 w 4.36 + 0.05 w 4.08 T 0.05 vs 3.94 + 0.05 s 3.79 + 0.05 m 3.54 + 0.03 w 3.45 + 0.03 w 3.33 + 0.03 w 3.28 + 0.02 w 3.22 + 0.02 w 3.01 + 0.02 m 2.95 + 0.02 w 2.82 + 0.02 w 2.74 + 0.02 w These X-ray diffraction data were collected with a Rigaku X-ray system, using copper K-alpha radiation. The positions of the peaks, expressed in degrees 2 theta, where theta is the Bragg angle, were determined by step-scanning at 0.02 degrees of 2 theta intervals and a counting time of 1 second for each step. The interplanar spacings, d, measured in Angstrom units (A), and the relative intensities of the lines, I/Io, where 10 is one-hundredth of the intensity of the strongest line, including subtraction of the background, were derived with the use of a profile fitting routine. The relative intensities are given in terms of the symbols vs = very strong (75-100%), s = strong (50-74%), m = medium (25-49%) and w = weak (0-24%). It should be understood that this X-ray diffraction pattern is characteristic of all the species of MCM-9 compositions synthesized by the present invention. Ion exchange of cat ions with other ions results in a silicophosphoaluminate which reveals substantially the same X-ray diffraction pattern with some minor shifts in interplanar spacing and variation in relative intensity. Other variations can occur, depending on the silicon/aluminum and phosphorus/aluminum ratios of the particular sample, as well as its degree of thermal treatment. The crystalline MCM-9 material of this invention may be converted to the dry, hydrogen form by the above thermal treatment of the organic cation-containing form or hydrogen ion precursor-containing form resulting from ion exchange. In general, the silicophosphoaluminate of the present invention can be prepared from a two-phase reaction mixture containing sources of aluminum, phosphorus and silicon, an organic directing agent(s) and a substantially water immiscible organic solvent. The overall molar composition of the two-phase synthesis mixture is in terms of oxides and organic components: ( )a:(M20)b:(A1203)c:(SiO2)d:(P205)e:(Solvent)f:(anion source)g where: a/(c+d+e) is less than 4, b/(c+d+e) is less than 2, d/(c+e) is less than 2, f/(c+d+e) is from 0.1 to 15, g/(c+d+e) is less than 2 and h/(c+d+e) is from 3 to 150. The "Solvent" is an organic solvent and "A" is any organic compound or material such as that derived from an organic directing agent or organic solvent. The anion is not necessarily separately added to the two-phase system, but may or may not appear in the product crystals from one or more of the other component sources. Reaction conditions consist of carefully heating the foregoing reaction mixture at a rate of from 5"C to 2000C per hour to a temperature of from 80"C to 300"C for a period of time of from 5 hours to 500 hours until crystals of IMCM-9 are formed. A more preferred temperature range is from 100"C to 200"C with the amount of time at a temperature in such range being from 24 hours to 168 hours. During heating and maintaining the reaction mixture at the desired temperature, the pH must be carefully controlled to be from 2 to 9. Control of pH can be accomplished byadjusting the concentrationof the added organic and/or inorganic base(s). The reaction is carried out until crystals of the desired MCM-9 form. The crystalline product is recovered by separating same from the reaction medium, as by cooling the whole to room temperature, filtering and washing with water before drying. The above reaction mixture composition can be prepared utilizing materials which supply the appropriate components. The aqueous phase components may include from the sources of the elements silicon, phosphorus, or aluminum, those not included in the organic phase. The organic phase comprises an organic solvent and a source of at least one of the elements silicon, phosphorus, or aluminum insoluble in the aqueous phase under reaction conditions. The aqueous phase also contains the required organic and/or inorganic directing agent(s). The useful sources of aluminum, as non-limiting examples, include any known form of aluminum oxide or hydroxide, organic or inorganic salt or compound. The useful sources of silicon include, as non-limiting examples, any known form of silicon dioxide or silicic acid, alkoxy- or other compounds of silicon. The useful sources of phosphorus include, as non-limiting examples, any known form of phosphorus acids or phosphorus oxides, phosphates and phosphites, and organic derivatives of phosphorus. The organic solvent is a C5-C10 alcohol or any other liquid compound substantially immiscible with water, as non-limiting examples. The organic directing agent can be selected from the group consisting of organic mono-, di- or polyamines and onium compounds having the following formula: or Or (R3M+R'M+R3)X2 wherein R or R' is alkyl of from 1 to 20 carbon atoms, heteroalkyl of from 1 to 20 carbon atoms, aryl, heteroaryl, cycloalkyl of from 3 to 6 carbon atoms, cycloheteroalkyl of from 3 to 6 carbon atoms, or combinations thereof; M is a tetracoordinate element (e.g. nitrogen, phosphorus, arsenic, antimony or bismuth) or a heteroatom (e.g. N, O, S, Se, P and As) in an alicyclic, heteroalicyclic or heteroaromatic structure; and X is an anion (e.g. fluoride, chloride, bromide, iodide, hydroxide, acetate, sulfate and carboxylate). When M is a heteroatom in an alicyclic, heteroalicyclic or heteroaromatic structure, such structure may be, as non-limiting examples, EMI10.1 wherein R' is alkyl of from 1 to 20 carbon atoms, heteroalkyl of from 1 to 20 carbon atoms, aryl, heteroaryl, cycloalkyl of from 3 to 6 carbon atoms or cycloheteroalkyl of from 3 to 6 carbon atoms. Particularly preferred directing agents for the present method include onium compounds, above defined, wherein R is alkyl of 1 to 4 carbon atoms, M is nitrogen and X is halide or hydroxide. Non-limiting examples of these include tetrapropylammonium hydroxide, tetraethylammonium hydroxide and tetrapropylammonium bromide. An inorganic hydroxide or salt of suitable composition can also be used as a supplemental directing agent, non-limiting examples of which are CsOH and KOH, CsCl and KC1. The MCM-9 crystals prepared by the instant invention can be shaped into a wide variety of particle sizes. Generally speaking, the particles can be in the form of a powder, a granule, or a molded product, such as an extrudate having particle size sufficient to pass through a 2 mesh (Tyler) screen and be retained on a 400 mesh (Tyler) screen. In cases where the catalyst is molded, such as by extrusion, the crystals can be extruded before drying or partially dried and then extruded. It may be desired to incorporate the new NCM-9 crystal with another material, i.e., a matrix, resistant to the temperatures and other conditions employed in various organic conversion processes. Such materials include active and inactive material and synthetic or naturally occurring zeolites as well as inorganic materials such as clays, silica and/or metal oxides, e.g. alumina. The latter may be either naturally occurring or in the form of gelatinous precipitates or gels including mixtures of silica and metal oxides. Catalyst compositions containing the MCM-9 crystals will generally comprise from 1% to 90% by weight of the MCM-9 material and from 10% to 99% by weight of the matrix material. More preferably, such catalyst compositions will comprise from 2% to 80% by weight of the NCM-9 material and from 2090 to 98% by weight of the matrix. Use of a material in conjunction with the new MCM-9 crystal, i.e. combined therewith, which is active, tends to alter the conversion and/or selectivity of the overall catalyst in certain organic conversion processes. Inactive materials suitably serve as diluents to control the amount of conversion in a given process so that products can be obtained economically and orderly without employing other means for controlling the rate of reaction. These materials may be incorporated into naturally occurring clays, e.g. bentonite and kaolin, to improve the crush strength of the catalyst under commercial operating conditions. Said materials, i.e. clays, oxides, etc., function as binders for the catalyst. It may be desirable to provide a catalyst having good crush strength because in commercial use it is desirable to prevent the catalyst from breaking down into powder-like materials. These clay binders have been employed normally only for the purpose of improving the crush strength of the overall catalyst. Naturally occurring clays which can be composited with the new crystal include the montmorillonite and kaolin families which include the subbentonites, and the kaolins commonly known as Dixie, McNamee, Georgia and Florida clays or others in which the main mineral constituent is halloysite, kaolinite, dickite, nacrite, or anauxite. Such clays can be used in the raw state as originally mined or initially subjected to calcination, acid treatment or chemical modification. In addition to the foregoing materials, the crystalline MCM-9 can be composited with a porous matrix material such as aluminum phosphate silica-alumina, silica-magnesia, silica-zirconia, silica-thoria, silica-beryllia, silica-titania as well as ternary compositions such as silica-alumina-thoria, silica-alumina-zirconia silica-alumina-magnesia and silica-magnesia-zirconia. The relative proportions of finely divided crystalline material and inorganic oxide gel matrix vary widely, with the crystal content ranging from 1 to 90 percent by weight and more usually, particularly when the composite is prepared in the form of beads, in the range of 2 to 80 weight percent of the composite. Employing a catalytically active form of the novel MCM-9 material of this invention as a catalyst component, said catalyst possibly containing additional hydrogenation components, reforming stocks can be reformed employing a temperature of from 370"C to 5400C, a pressure of from 100 psig to 1000 psig (791 to 6996 kPa), preferably from 200 psig to 700 psig (1480 to 4928 kPa), a liquid hourly space velocity is from 0.1 to 10, preferably from 0.5 to 4, and a hydrogen to hydrocarbon mole ratio of from 1 to 20, preferably from 4 to 12. A catalyst comprising the present MCM-9 material can also be used for hydroisomerization of normal paraffins, when provided with a hydrogenation component, e.g. platinum. Such hydroisomerization is carried out at a temperature of from 90"C to 375"C, preferably from 145"C to 2900C, with a liquid hourly space velocity of from 0.01 to 2, preferably from 0.25 to 0.50, and with a hydrogen to hydrocarbon mole ratio of from 1:1 to 5:1. Additionally, such a catalyst can be used for oleo in or aromatic isomerization, employing a temperature of from 200"C to 4800C. Such a catalyst can also be used for reducing the pour point of gas oils. This reaction is carried out at a liquid hourly space velocity of from 10 to 30 and at a temperature of from 425"C to 5950C. Other reactions which can be accomplished employing a catalyst comprising the MCM-9 of this invention containing a metal, e.g. platinum, include hydrogenation-dehydrogenation reactions and desulfurization reactions, oleo in polymerization (oligomerization) and other organic compound conversions, such as the conversion of alcohols (e.g. methanol) or ethers (e.g. dimethylether) to hydrocarbons, and the alkylation of aromatics (e.g. benzene) in the presence of an alkylating agent (e.g. ethylene). In order to more fully illustrate the nature of the invention and the manner of practicing same, the following examples are presented. In the examples, whenever adsorption data are set forth for comparison of sorptive capacities for various adsorbants, they were determined as follows: A weighed sample of the calcined adsorbant was contacted with a flowing stream of the equilibrium vapor of the adsorbate at 250C, admixed with dry nitrogen. Msorbates were water vapor and n-hexane, 2-methylpentane, xylene or cyclohexane vapors. The sample temperature was maintained at 900C for adsorbates other than ortho-xylene for which it was 1200C and water for which it was 60"C. The increase in weight was measured gravimetrically and converted to the adsorption capacity of the sample in weight percent of calcined adsorbant. When Alpha Value is examined, it is noted that the Alpha Value is an approximate indication of the catalytic cracking activity of the catalyst compared to a standard catalyst and it gives the relative rate constant (rate of normal hexane conversion per volume of catalyst per unit time). It is based on the activity of the highly active silica-alumina cracking catalyst taken as an Alpha of 1 (Rate Constant = 0.016 sec 1). In the case of zeolite HZSM-5, only 174 ppm of tetrahedrally coordinated A1203 are required to provide an Alpha Value of 1. The Alpha Test is described in U.S. Patent 3,354,078 and in The Journal of Catalysis, Vol. IV, pp. 522-529 (August 1965). When ion-exchange capacity is examined, it is determined by titrating with a solution of sulfamic acid the gaseous ammonia evolved during the temperature programmed decomposition of the ammonium-form of the silicophosphoaluminate. The method is described in Thermochimica Acta, Vol. III, pp. 113-124, 1971 by G.T. Kerr and A.W. Chester. E)CMPLE 1 A two-phase synthesis reaction mixture was prepared with the organic phase comprised of lOg Si(OC2H5)4 and 60g l-hexanol, and the aqueous phase comprised of 23.lg H3PO4 (85%), 13.7g A1203, l0.lg di-n-propylamine and 59.6g of H20. The reaction mixture as a whole had a composition including 9.3% Si, 38.8% P and 51.9% awl, the percentages atomic. The directing agent was di-n-propylamine. Starting pH was between 5 and 7. The reaction mixture was heated at 500C per hour to 130"C and maintained at that temperature for 24 hours. It was then heated to 200"C and maintained at that temperature for 24 hours until crystals of silicophosphoaluminate formed. The crystalline product was separated from the reaction mixture by filtration, water washed and then dried at 80"C. The product crystals were analyzed to contain 13.1% Si, 42.7% P and 44.2% Al, percentages atomic. A sample of the as synthesized silicophosphoaluminate was then submitted for X-ray analysis and found to be a molecular sieve structure exhibiting the diffraction lines shown in Table 2. Table 2 Observed Relative Intensities Interplanar d-Spacings (A) 2 x Theta 111o 16.4111 5.381 62.39 10.8526 8.140 17.66 9.6576 9.149 32.12 9.3204 9.481 27.26 8.2047 10.774 20.52 6.8566 12.901 76.05 6.7054 13.193 12.08 6.4892 13.634 54.07 6.1653 14.354 10.73 5.6353 15.712 26.80 5.4550 16.235 4.23 4.8496 18.278 59.79 4.7388 18.710 14.59 4.6681 18.996 5.63 4.3551 20.375 49.35 4.2273 20.998 92.67 4.1353 21.471 37.27 4.0810 21.759 100.00 4.0106 22.146 27.79 3.9298 22.607 47.48 3.8322 23.191 40.95 3.7598 23.644 14.34 3.6060 24.668 14.55 3.3878 26.285 31.22 3.3439 26.636 9.32 3.2759 27.199 24.92 3.1640 28.180 13.98 3.0649 29.112 65.46 2.9449 30.325 18.46 2.8926 30.887 20.58 2.8367 31.512 7.14 2.7792 32.181 9.79 2.7311 32.764 15.65 2.6815 33.388 32.91 2.6183 34.218 8.19 <RTI ID=17.1> EYRMPLE 2 The synthesis of Example 1 was repeated except that the reaction mixture was kept at 2000C for 48 hours. The crystalline silicophosphoaluminate was analyzed to contain 14.5% Si, 42.4%P and 43.1% Al, percentages atomic. A sample of the as-synthesized silicophosphoaluminate was submitted for X-ray analysis and found to be a molecular sieve structure exhibiting the diffraction lines shown in Table 3. Table 3 Observed Relative Intensitites Interplanar d-Spacings (A) 2 x Theta I/Io 16.4079 5.382 100.00 10.8449 8.146 7.49 9.3382 9.463 14.69 8.2045 10.774 30.68 6.6779 13.247 7.67 6.1687 14.346 14.01 5.6460 15.683 12.66 5.4639 16.209 5.08 4.8358 18.331 3.08 4.7403 18.704 14.29 4.3370 20.461 14.88 4.2142 21.064 54.04 4.0922 21.699 28.93 4.0529 21.912 33.05 4.0066 22.169 16.42 3.9361 22.571 42.98 3.8330 23.186 25.28 3.7675 23.595 20.32 3.6367 24.457 7.76 3.5884 24.791 8.64 3.3881 26.282 5.67 3.3420 26.651 3.81 3.2787 27.176 32.35 3.1646 28.175 9.66 3.0888 28.881 13.52 3.0304 29.451 9.22 2.9527 30.244 19.34 2.8974 30.835 9.66 2.8383 31.494 3.59 2.7410 32.642 15.87 2.6273 34.097 6.96 EXAMPLE 3 A quantity of the crystalline silicophosphoaluminate of Example 2 was calcined at 4500C in nitrogen for 4 hours and then X-ray analyzed. The results are presented in Table 4. Table 4 Observed Relative Intensities Interplanar d-Spacings (A) 2 x Theta 1/1o 16.3622 5.397 47.46 14.0545 6.284 21.20 10.9231 8.088 6.38 8.9443 9.881 41.09 8.1901 10.793 9.93 6.9002 12.819 13.13 5.4998 16.102 29.83 4.4683 19.853 22.63 4.3595 20.354 7.28 4.0790 21.770 100.00 3.9420 22.537 59.93 3.7815 23.507 34.47 3.5387 25.145 18.20 3.4518 25.788 10.08 3.3277 26.768 7.78 3.2785 27.177 13.51 3.2215 27.668 7.00 3.0139 29.615 33.24 2.9487 30.286 11.29 2.8231 31.668 7.73 2.7398 32.657 18.39 EXAMPLE 4 A quantity of the crystalline silicophosphoaluminate of Example 1 was calcined as described in Example 3 and ammonium-exchanged using a 1M NH4NO3 solution. The ion-exchange capacity measured from the evolution of ammonia was determined to be 0.22 meq/g. EXAMPLE 5 Thus ion-exchange capacity of the crystalline silicophosphoaluminate of Example 2 was determined as described in Example 4. It was equal to 0.105 meq/g. EXAMPLE 6 A quantity of the crystalline silicophosphoaluminate of Example 5 was tested in Alpha Test. Its Alpha value was 1.4 EXAMPLE 7 A quantity of the crystalline silicophosphoaluminate of Example 5 was used to conduct the constraint index test (described in U.S. Patent 4,385,195, entirely incorporated herein by preference). The constraint index was 0.4, indicating the presence of large pores. EXAMPLE 8 A sample of the calcined product crystalline silicophosphoaluminate of Example 1 was evaluated for sorption properties to confirm its molecular sieve nature. The results in weight percent were as follows: water (60"C): 1.73 n-hexane (90"C): 1.00 EXAMPLE 9 A sample of the calcined product of Example 2 was also evaluated for sorption properties. The results in weight percent were as follows: water (60"C) 3.8 n-hexane (900C) 1.1

Claims: CLAIMS: 1. A synthetic crystalline material comprising silicon, phosphorus and aluminum which, as synthesized, exhibits a characteristic X-ray diffraction pattern as shown in Table 1-A of the specification. 2. The synthetic crystalline material of Claim 1 which, following calcination, exhibits a characteristic X-ray diffraction pattern as shown in Table 1-B of the specification. 3. The synthetic crystalline material of Claim 1 having a composition as follows: vA:M###:(A1O2)-1-y:(PO2)+1-x:(SiO2)x+y:N###:wH2O wherein M is a cation of valence m, N is a cation of valence n, A is an organic material, v is the number of moles of A, w is the number of moles of H2O and x and y are numbers of from greater than -1 to less than +1 which satisfy the relationships: (1) if x is 0, then y is not 0, (2) if y is 0, then x is not 0, and (3) x + y is greater than 0.001 and less than 1. 4. The synthetic crystalline material of Claim 2 having a composition in the anhydrous state as follows: Mm###:(A1O2)-1-y:(PO2)+1-x:(SiO2)x+y:N###n wherein M is a cation of valence m, N is an anion of valence n, and x and y are numbers of from greater than -1 to less than +1 which satisfy the relationships: (1) if x is 0, then y is not 0, (2) if y is 0, then x is not 0, and (3) x + y is greater than 0.001 and less than 1. 5. The crystalline material of any of Claims 1 to 4 having original cations replaced, at least in part, with a cation or a mixture of cations selected from the group consisting of hydrogen and hydrogen precursors, rare earth metals and metals from Groups IA, IIA, II IA, IVA, IB, IIB, IIIB, IVB and VIII of the Periodic Table of the Elements. 6. The crystalline material resulting from thermal treatment of the crystalline material of Claim 5. 7. A catalyst composition comprising from 1% to 90% by weight of the crystalline material of any of Claims 1 to 6 and from 10% to 998 by weight of a matrix material. 8. Use of the crystalline material or composition of any of Claims 1 to 7 as a catalyst for the conversion of organic compounds.

Inventors: DEROUANE, ERIC GERARD, VON BALLMOOS, ROLAND (NMN)
Applicants: MOBIL OIL CORPORATION
Application year: 1984
Main classification: C01B33
IPC codes: B01J29, C01B37, B01J39, B01J20