METHOD OF PREPARING ZEOLITE ZSM-48, THE ZEOLITE SO PREPARED AND ITS USE AS CATALYST FOR ORGANIC COMPOUND CONVERSION

Abstract: A method of preparing the zeolite ZSM-48 (defined by lattice structure and X-ray data). The method prescribes a reaction mixture defined by particular values for Al₂O₃/SiO₂, Na₂O SiO₂, RN SiO₂, OH-/SiO₂ and H₂O/SiO₂, RN being a C₂-C₁₂ alkylamine compound or a quaternary ammonium compound or mixture thereof. A compositional formula for zeolites prepared according to the invention is provided and their use as catalysts and sorbents is demonstrated.

Description: METHOD OF PREPARING ZEOLITE ZSM-48, THE ZEOLITE SO PREPARED AND ITS USE AS CATALYST FOR ORGANIC COMPOUND CONVERSION This invention relates to a method for the preparation of the relatively new zeolite designated ZSM-48 and to the zeolite so prepared. The zeolite, which is one of those which can be prepared from reaction mixtures to which no aluminium has been added, is described in our copending European Application No. 80300463. The SiO2/A1203 ratio of a given zeolite is often variable. For example, zeolite X can be synthesized with SiO2/A1203 ration from 2 to 3; zeolite Y, from 3 to about 6. In some zeolites the upper limit of SiO2/A1203 ratio is unbounded. ZSM-5 is one such example wherein SiO2/A1203 ratio is at least five. U.S. Patent 3,941,871 discloses a crystalline metal organosilicate essentially free of aluminium and exhibiting an X-ray diffration pattern characteristic of ZSM-5 type aluminosilicates. U.S. Patents 4,061,724, 4,073,865 and 4,104,294 describe microporous, crystalline silicas or organosilicates. According to our aforesaid prior European Application ZSM-48 is defined as a crystalline zeolitic material having a lattice comprising Si04 tetrahedra crosslinked by the sharing of oxygen atoms and characterized by the following interplaner spacings manifested by the zeolite in the calcined, sodium-exchanged form: TABLE 1 d(A) Relative Intensity (I/IoA 11.8 + 0.2 S 10.2 + 0.2 W-M 7.2 + 0.15 W 4.2 + 0.08 VS 3.9 + 0.08 VS 3.6 + 0.06 W 3.1 + 0.05 w 2.85 + 0.05 W These values were determined by standard techniques. The radiation was the K-alpha doublet of copper, and a diffractometer equipped with a scintillation counter and a strip chart pen recorder was used. The peak heights, I, and the positions as a function of 2 times theta, where theta is the Bragg angle, were read from the spectrometer chart. From these, the relative intensities, 100 I/Io, where 10 is the intensity of the strongest line or peak, and d (obs.), the interplanar spacing in A, corresponding to the recorded lines, were calculated. In Table 1 the relative intensities are given in terms of the symbols W = weak, VS = very strong, M = medium and W-S = weak-to-strong (depending on the cationic form). Ion exchange of the sodium ion with cations reveals substantially the same pattern with some minor shifts in interplanar spacing and variation in relative intensity. Other minor variations can occur depending on. the silicon to aluminium ratio of the particular sample, as well as if it has been subjected to thermal treatment. When synthesised according to the preferred techniques disclosed in our prior European Application ZSM-48 usually crystallized in a form satisfying the formula, in mole ratios of oxides: (O to f5)RN:(O to 1.5)M20:(O to 2)A1203:(100)SiO2 n in which M is at least one cation of valance n and RN is a C1-C20 organic compound having at least one amine functional group of peak7. According to the present invention a different route to synthesis of ZSM-48 is provided, the zeolite being prepared from a reaction mixture containing a source of silica, RN, an alkali metal oxide, e.g. sodium, with or without a source of alumina, and water, and having a composition, in terms of mole ratios of oxides, falling within the following ranges: REACTANTS BROAD PREFERRED A12O3/SiO2 = O to 0.08 0 to 0.02 Na2O/Sib2 = 0.01 to 1.0 0.1 to 0.5 RN/SiO2 = 0.01 to 1.0 0.1 to 0.5 OH-/SiO2 = 0.01 to 0.5 0.05 to 0.2 H2O/SiO2 = 10 to 200 20 to 100 wherein RN is a C2-C12 alkylamine or a quaternary ammonium compound or mixtures or mixtures thereof, and maintaining the mixture at 80-200 C until crystals of the new material are formed. For the purposes of the present specification ZSM-48 remains defined as it was in our aforesaid prior European Application, namely by its X-ray diffraction data. However a convenient compositional formula which embraces most forms of the zeolite synthesised by the method of the present invention, in terms of moles of anhydrous oxides per 100 moles of silica, is as follows: (0.1 to 10)RN : (0.1 to 10)M2/nO : (O to 4)A12O3 (100)SiO2 wherein This is at least one cation having a valence n, RN is a C-C12 alkylamine or a quaternary ammonium compound or mixtures thereof. The original cations of the zeolite can be replaced, at least in part, by calcination and/or ion exchange with another cation. Thus, the original cations are exchanged into a hydrogen or hydrogen ion precursor form or a form in which the original cation has been replaced by a metal of Groups 2- through 8 of the Periodic Table. Thus, for example, it is contemplated to exchange the original cations with ammonium ions or with hydronium ions. Catalytically active forms of these would include, in particular, hydrogen, rare earth metals, aluminium, metals of Groups II and VIII of the Periodic Table and manganese. ZSM-48 can also be used as a catalyst in intimate combination with an additional hydrogenating component such as tungsten, vanadium, molybdenum, rhenium, nickel, cobalt, chromium, manganese, or a noble metal such as platinum or palladium where a hydrogenation-dehydrogenation function is to be performed. Such component can be exchanged into the composition, to the extent as in the structure, impregnated therein or physically intimately admixed therewith. Such component can be impregnated, in or on to it such as, for example, by, in the case of platinum, treating the silico-crystal with a solution containing a platinum metal-containing ion. Thus, suitable platinum compounds include chloroplatinic acid, platinous chloride and various compounds containing the platinum ammine complex. Especially in its metal, hydrogen, ammonium, alkylammonium and arylammonium forms the zeolite can be beneficially converted to another form by thermal treatment. This thermal treatment is generally performed by heating one of these forms at a temperature of at least 700 F for at least 1 minute and generally not greater than 20 hours. While subatmospheric pressure can be employed for the thermal treatment, atmospheric pressure is desired for reasons of convenience. The thermal treatment can be performed at a termperature of 1700"P. The thermally treated product is particularly useful in the catalysis of certain hydrocarbon conversion reactions. When employed either as an absorbent or as a catalyst in one of the aforementioned processes zeolite ZSM-48 should be dehydrated, at least partially. This can be done by heating to a temperature in the range of 200 to 600"C in an atmosphere, such as air, nitrogen, etc. and-at atmospheric, subatmospheric or superatmospheric pressures for between 1 and 48 hours. Dehydration can also be performed at room temperature merely by placing the zeolite in a vacuum, but a longer time is required to obtain a sufficient amount of dehydration. Preferably, crystallization is carried out under pressure in an autpclave or static bomb reactor, at 80 to 200"C. Thereafter, the crystals are separated from the liquid and recovered. The composition can be prepared utilizing materials which supply the appropriate oxide. Such compositions include sodium silicate, silica hydrosol, silica gel, silicic acid, sodium hydroxide, chromic potassium sulfate. The zeolite prepared by the present invention may form in 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 sixe sufficient to pass through a 2 mesh (Tyler) screen and be retained on a 400 mesh (Tyler) screen. In cases where a catalyst is molded, such as by extrusion, the zeolite can be extruded before drying or dried or partially dried and then extruded. For catalytic usage ZSM-48 may be composited with a matrix such as described in our European Specification 0,001,695. In order to more fully illustrate the nature of the invention and the manner of practising same, the following examples are presented, wherein porous ZSM-48 crystals of good crystallinity were prepared from mixes of the composition range: (1 to 100)RN : (1 to 100)Na2O : (O to 8)A1205 100 SiO2 : (1000 to 20,000)H20 wherein RN is a C2-C12 alkylamine, a quaternary ammonium compound or a mixture of the above form. Adsorption data were determined as follows: A weighed sample of the calcined composition was contacted with the desired pure adsorbate vapor in an adsorption chamber, evacuated to less than one mm Hg and then contacted with 12 mm Hg of water vapor or 20 mm Hg of cyclohexane or n-hexane vapor, pressures less than the vapor-liquid eqilibrium pressure of the respective adsorbate at room temperature. The pressure was kept constant (within about + 0.5 mm) by addition of adsorbate vapor controlled by a manostat during the adsorption period which did not exceed about eight hours. As the adsorbate was adsorbed by the zeolite, the decrease in pressure caused the manostat to open a valve which admitted more adsorbate vapor to the chamber to restore the above control pressures. Sorption was complete when the pressure change was not sufficient to activate the manostat. The increase in weight was calculated as the adsorption capacity of the sample. EXAMPLE 1 A silicate solution comprising 1718 grams of Q-brand sodium silicate (28.8% siO2, 8.9% Na20, 62% K20) and 4000 g of water, a acid solution comprising 172 g of H2S04. Six hundred g of 50% wt. tetramethylammonium chloride and 4100 g H20, and 800 g of n-propylamine, were charged to a 5-gallon autoclave the silicate and acid solutions being charged first. After approximately 46 hours at 3200F with 90 rpm agitation, the reaction mixture crystallized into a product of mainly ZSM-48 material, in the shape of needles. Some other material was also found, octahedral in shape, apparently a metastable precursor of ZSM-48. Elemental analysis was as follows: Na 0.27% Si 93.2% Al 0.40% N 0.18% Adsorption Capacity was as follows: H20 1 .8% Cyclohexane 0.3% n-hexane 3.7 The following Table II shows the x-ray diffraction data of the product after separation to remove impurities and calcination. TABLE II X-Ray Data For Product Of Example 1 Calcined 21 hours at 50000 2 times theta D(A) 100 I/Io 7.48 11.82 74 8.67 10.20 29 12.30 7.20 7 12.83 6.90 3 14.50 6.11 7 * 15.10 5.87 20 * 15.78 5.62 4 16.75 5.29 1 17.55 5.05 2 18.14 4.89 2 18.60 4.77 1 19.02 4.67 1 19.90 4.46 2 20.52 4.33 2 21.06 4.22 82 21.75 4.09 9 22.25 4.00 8 22.83 3.90 100 23.80 3.74 3 24.55 3.63 3 24.80 3.59 4 25.70 3.47 3 26.45 3.37 4 * 27.22 3.28 4 27.67 3.22 1 29.02 3.08 4 30.67 2.91 1 31.36 2.85 14 32.77 2.73 3 34.12 2.63 2 35.62 2.52 3 36.13 2.49 3 36.48 2.46 4 37.85 2.38 4 38.30 2.35 3 40.30 2.24 2 43.05 2.10 3 44.00 2.06 3 * Intensity due to or enhanced by other components(s). EXAMPLE 2 Fifty grams of the dried zeolite product from Example 1 were calcined in N2 stream at 100off for 3 hours to decompose most of the organics associated with the zeolite. Two NH4 ion exchanges were carried out at room temperature with Scc of 1 NNH4N03 solution per gram of sample for one hour each to reduce Na level of the sample to < 0.02 wt. %. The ion exchanged sample was washed, dried and sized to 14/25 mesh prior to the final air activation step of 3 hours at 1000 F. One cc of the above activated sample was tested for its hydrocarbon-cracking activities by the standard alpha-test* and was found to have an alpha-value of 6.4. (The alpha test is described in Journal of Catalysis, Vol. 4, pp. 522-529 (August 1965)). EXAMPLE 3 Five grams of the dried zeolite product from Example 1 were calcined in N2 stream at 1000ref for 3 hours. The calcined sample was ion exchanged twice with a mixed solution of 100 ml 0.iN NaC1 and 50 ml 0.1N NaOH at room temperature for one hour each. The Na form sample was filtered, water washed and finally dried at 230 ? for at least 3 hours. The X-ray diffraction data of the calcined sodium-exchanged product is given below in Table III. TABLE 3 2 Times theta D(A) 100I/Io 7.55 11.71 51 8.72 10.14 22 12.36 7.16 6 12.93 6.85 3 14.54 6.09 8 * 15.14 5.85 21 * 15.84 5.59 5 17.60 5.04 3 18.17 4.88 4 18.68 4.75 2 19.10 4.65 2 19.56 4.54 2 20.02 4.44 4 20.48 4.34 4 21.09 4.21 74 21.72 4.09 11 22.22 4.00 11 22.88 3.89 100 * 23.89 3.72 10 24.47 3.64 5 24.89 3.58 10 25.38 3.51 7 25.80 3.45 7 26.17 3.41 4 26.52 3.36 8 * 27.22 3.28 5 29.06 3.07 3 30.72 2.91 1 31.40 2.85 11 32.65 2.74 1 32.98 2.72 2 33.53 2.67 1 34.19 2.62 1 35.67 2.52 2 36.20 2.48 3 36.60 2.46 2 37.06 2.43 2 37.55 2.40 2 37.94 2.37 4 38.34 2.35 2 39.52 2.28 1 40.30 2.24 1 43. 1 0 2. 1 0 2 44.06 2.06 2 * Intensity due to or enhanced by other components(s).

Claims: CLAIMS 1. A method of preparing zeolite ZSM-48 which comprises preparing a reaction mixture containing a source of a silica, an alkali metal oxide, RN, and water and having a composition, in terms of mole ratios of oxides, falling within the following ranges: A1203/SiO2 = O to 0.08 Na2O/Si02 = 0.01 to 1.0 RN/SiO2 = 0.01 to 1.0 OH-/SiO2 = 0.01 to 0.5 H20/SiO2 = 10 to 200 wherein RN is a C2-C12 alkylamine compound or a quaternary ammonium compound or mixtures thereof, and maintaining said mixture until crystals of the zeolite are formed. 2. A method according to claim 1 wherein the reaction mixtures has a composition, in terms of mole ratios of oxides, falling within the following ranges: A1203/SiO2 = O to 0.02 Na2O/SiO2 = 0.1 to 0.5 RN/Si02 = 0.1 to 0.5 OH-/SiO2 = 0.05 to 0.2 H20/SiO2 = 20 to 100 3. A method according to claim 1 or claim 2 wherein RN comprises a n-propyl amine and tetramethylammonium chloride. 4. A method according to any of claims 1 to 3 wherein said reaction mixture is maintained at a temperature of 80 to 200"C until said crystals are formed. 5. Zeolite ZSM-48 whenever prepared by the method claimed in any of claims 1 to 4. 6. A process for converting organic compounds which comprises contacting such compounds, under conversion conditions, with a catalyst comprising zeolite ZSM-48 as claimed in claim 5.

Inventors: CHU, POCHEN
Applicants: MOBIL OIL CORPORATION
Application year: 1980
Main classification: C01B33
IPC codes: C01B39, B01J29, C01B37