BARIUM TITANATE- CONTAINING FLUIDIZABLE CRACKING CATALYST COMPOSITION

Abstract: There is disclosed a cracking catalyst composition comprising a zeolitic, crystalline aluminosilicate, a matrix material and a barium titanium oxide. The catalyst composition is particularly suitable for cracking metal-containing hydrocarbon feed stocks.

Description: The invention relates to a fluidizable cracking catalyst composition comprising a zeolitic, crystalline aluminosilicate, a matrix material and a barium compound. A catalyst composition of this type is suitable for cracking oil feedstocks and is disclosed in United States Patent Specification 4 473 463. According to the description in it barium compounds are incorporated into or applied onto cracking catalysts to prevent deleterious effects caused by metals contaminations in oil feedstocks. The catalysts generally contain a silica-alumina matrix in which zeolitic materials are embedded. Preferably, use is made of barium acetyl acetonate. In said patent specification the results obtained with it are described in an example in which a cracking catalyst contaminated with metals is re-activated in a treatment with barium acetyl acetonate. This compound, however, and many other barium compounds are not quite suitable to be used for composing a metal resistant cracking catalyst, as appears from metal resistance and micro-activity tests (referred to as MR test and MAT test, respectively). A barium compound has now been found which does not show the above drawback. The invention consists in that the cracking catalyst composition of the above well-known type contains a barium titanium oxide. Use of barium compounds in cracking catalysts is also known from other patent specifications. US 4 179 409 describes a cracking catalyst which in addition to a zeolite and an inorganic oxyde gel matrix contains a perovskite. As a result, the cracked oil will have a higher octane number. The perovskite may be a barium compound, such as barium zirconate (BaZrO₃). In the cracking process of EP 0 063 712 use is made of metal traps, such as type A zeolite, which may contain for instance a barium compound. It should be added that US 4 451 355 relates to a cracking catalyst which in addition to a zeolitic aluminosilicate and a matrix material contains a calcium-containing additive for trapping metals contaminations. Particular calcium/titanium-containing compounds, amongst which calcium titanate (CaTiO₃), are considered to be particularly suitable for this purpose. The barium titanium oxides that may be included in the present catalyst composition are described by, int.al., D.E. Rase and R. Roy in J. Amer. Ceram. Soc. 38 , 108 (1955), by G.H. Jonker and W. Kwestroo in J. Amer. Ceram. Soc. 41 , 390 (1958) and by H.M.O'Bryan and I. Thomson in J. Amer. Ceram. Soc. 57 , 522(1974). As examples of suitable barium titanium oxides may be mentioned Ba₂TiO₄, BaTiO₃, Ba₂Ti₅O₁₂, Ba₆TO₁₇O₄₀, BaTi₃O₇, Ba₄Ti₁₃O₃₀, BaTi₄O₉ and Ba₂Ti₉O₂₀. Particularly suitable are Ba₂TiO₄, BaTi₃O₇ and especially BaTiO₃ (barium titanate). As zeolite crystalline aluminosilicate may be used all molecular sieves commonly employed for cracking catalysts. It is preferred that use should be made of synthetic crystalline aluminosilicates having a pore diameter in the range of 3 to 15 angstroms. Examples thereof include the zeolites A, X, Y, ultrastabilized sieves, ZK-4, ZK-5, ZSM-5, ZSM-11 ans ZSM-12. It is preferred that zeolites of the types X, Y and/or ultrastabilized sieves should be applied. To ensure proper catalyst activity the cations of these zeolites, which are often prepared in the sodium form, need be exchanged. For this ion exchange use is generally made of solutions containing rare earth metal ions and/or ammonium or hydrogen ions. The exchange is as a rule carried on to such a level that the zeolites and the ready catalyst contain less than 4% by weight, preferably less than 0,5% by weight of sodium. As matrix material can be used all well-known matrix materials suitable for embedding zeolitic, crystalline aluminosilicates, such as silica, alumina, magnesia, zirconia, titania, boria, aluminium chlorohydrol and mixtures thereof. Preference is given to silica, silica-alumina and alumina. In addition to the barium titanium oxide and the alumino silicate other components may be incorporated into the matrix material. As examples thereof may be mentioned clays such as kaolin, bentonite and layered clays as discussed in U.S. Patent Specifications 3 252 757, 3 252 889 and 3 743 594, montmorrilonite, etc. To augment the octane number of the petrol fraction produced alumina particles as described in U.S. Patent Specification 4 182 693 may be incorporated into the catalyst composition. Moreover, use may be made of usual amounts of one or more passivators which may contain antimony, tin, and the like. They particularly serve to prevent excessive formation of hydrogen during the cracking process. To reduce SO x emission and to promote the conversion of CO to CO₂ an oxidation promoting metal or metal compound may be incorporated into the present composition. The cracking catalyst composition generally contains 0,05-1000 ppm of an oxidation promoting metal or metal compound. Suitable for that purpose are noble metals or compounds thereof of group VIII of the periodic system, such as Pt, Pd, Ir, Rh, Os and Ru. Also suitable to that end are rare earth metals or compounds thereof. Examples of suitable oxidation promoters also include Cr and Cu, and compounds thereof. It is preferred that use should be made of 0,1 to 100 ppm, more particularly 0,1-50 ppm, of a noble metal of group VIII. Most preference is given to the incorporation into the catalyst of 0,1-10 ppm of platinum or palladium. These metals may be incorporated in the catalyst in a known manner, for instance by impregnation with a corresponding salt solution. The components of the catalyst composition may be combined with the matrix material in a manner known in itself. Suitable methods of preparation are described, among other places, in U.S. Patent Specifications 3 609 103 and 3 676 330. For instance, the barium titanium oxide and the aluminosilicate may be combined with the matrix material when the latter material is already in the gelled state. After proper mixing and subsequent spray drying the ready catalyst composition is obtained. Alternatively, the various components may be added to a matrix material in the form of a sol. This sol bonding agent can be formed into a gel before or during spray drying. The latter procedure is to be preferred in that it permits obtaining catalyst compositions having a relatively high density. Thus, apparent densities higher than 0,5 g/ml, preferably higher than 0,70 g/ml are simple to realize. A suitable catalyst composition according to the present invention comprises 5-50, preferably 10-30 per cent by weight of a zeolitic, crystalline aluminosilicate and 0,01-30, preferably 1-20, more particularly 1-10 per cent by weight of barium titanium oxide, which two components are embedded in 10-90 per cent by weight of matrix material. It is preferred that the aluminosilicate should consist of a type Y zeolite or an ultrastabilized zeolite exchanged for rare earth metal ions and/or ammonium or hydrogen ions. As matrix material there is preferably used a silica, silica-alumina or alumina formed into a gel by spray drying the total composition. Particularly in uses requiring a reduction of SO x emission it is preferred that into the catalyst composition there should be incorporated 0,1-10 ppm of platinum. The cracking catalyst composition may optionally consist of a physical mixture of: a. catalytically active particles comprising a zeolitic, crystalline aluminosilicate embedded in matrix material, and b. catalytically less active particles comprising barium titanium oxide embedded in matrix material. This embodiment of the invention has the advantage that the amount of barium titanium oxide added can readily be adapted to the feedstock to be cracked. Very suitable is a physical mixture in which: a. the catalytically active particles contain 10-80, preferably 20-40 per cent by weight of zeolitic, crystalline aluminosilicate, 5-60, preferably 20-50 per cent by weight of clay and 5-85, preferably 10-30 per cent by weight of silica, silica-alumina or alumina, and b. the catalytically less active particles contain 10-80, preferably 10-40 per cent by weight of barium titanium oxide, and 10-90, preferably 10-30 per cent by weight of silica, silica-alumina, or alumina and, optionally, 10-50 per cent by weight of clay. Also in this mixture the silica, silica-alumina or alumina in the catalytically active and/or less active particles preferably consists of silica, silica-alumina or alumina formed into a gel by spray drying the respective particles. Especially if augmentation of the octane number of petrol fractions is envisaged, then aluminium oxide particles may be incorporated into the catalytically active and/or less active particles in an amount of up to in all 40, preferably 1-15 per cent by weight of aluminium oxide particles. It is also possible for the two different types of particles to have different diameters. For instance, the catalytically active particles may have a diameter of 80-125 microns and the catalytically less active particles a diameter of 30-75 microns. Moreover, into one or more of the two components of the mixture a noble metal of group VIII of the periodic system may be incorporated in a concentration of 0,1-100 ppm, preferably 0,1 to 50 ppm, calculated on the weight of the total mixture. It is again preferred then that the platinum should be used in an amount of 0,1-10 ppm. The present catalyst composition is suitable for use in a conventional process for cracking feeds. Catalytic cracking is normally carried out at a temperature of 375°-650°C, more particularly 460°-560°C. The pressure applied is generally in the range from atmospheric pressure to a pressure of 7 atmospheres, more particularly a pressure from 1 to 3 atmospheres. Regeneration with steam is generally carried out at 540°-825°C, more particularly 750°-800°C. As feeds may be used the hydrocarbon materials that are normally subjected to cracking. The catalyst composition is particularly suitable for cracking metal-containing hydrocarbon feed stocks having a boiling range which generally ends at a temperature higher than 480°C, a density greater than 900 kg/cm³, a metal concentration (Ni and V) of more than 1 ppm and a Conradson carbon content higher than 1%. The present catalyst composition, however, is preferably applied to heavier feeds, such as residues that include a substantial concentration of metals and/or asphaltenes. If the feedstock has a high metal content, preference is given to a process in which the feedstock to be cracked is first brought into contact with the barium titanium oxide-containing particles and subsequently with the zeolite-containing particles. The feedstock will be demetallized then before cracking. Example 1 The catalyst compositions in Table 1 were obtained by mixing the various catalyst constituents with a silica-alumina sol. The total composition was milled in a colloid mill, gelled by spray drying, and the resulting particles were exchanged with (NH₄)₂SO₄, and dried. The performance of the resulting catalyst compositions was measured by carrying out MAT and MR tests. The MAT test corresponds to test method D3907-80 of the American Society for Testing and Materials (ASTM). The MR test is described on pp 80-84 of the Ketjen Symposium book, 1982, Amsterdam, The Netherlands. The MAT and the MR tests are used for determining the activity of the cracking catalyst prior to (MAT test) and after (MR test) contamination of the catalyst with metals (nickel and vanadium). The higher the rate constant k and the conversion, the more active the catalyst will be. The results mentioned in Table 2 illustrate the extraordinary effectiveness of catalysts containing a barium titanium oxide, in particular barium titanate. The results also show that the amount of barium titanium oxide in the total catalyst composition can be varied within wide limits. For comparison the table gives the test results obtained with additives that are known from the state of the art discussed hereinbefore. Example 2 Use being made of the procedure described in Example 1, catalysts A and B were prepared that contain an ultrastable Y-zeolite and are further characterized by the composition and properties mentioned in the table below. The test results in the following Table IV show the excellent resistance to metal (see MR test) of catalyst B, which contains barium titanate. Example 3 Use being made of the procedure described in Example 1 the following Y-zeolite-containing "active" and barium titanate-containing "less active" catalyst particles were prepared. Then a mixture was prepared of equal amounts by weight of the two types of particles. The mixture contained 1,6% RE₂O₃, 0,25% Na₂O and had an SA=109m²/g. The MAT and MR test results show the effectiveness of this cracking catalyst mixture.

Claims: 1 A fluidizable cracking catalyst composition comprising a zeolitic, crystalline aluminosilicate, a matrix material and a barium compound, characterized in that the barium compound is a barium titanium oxide. 2 A fluidizable cracking catalyst composition according to claim 1, characterized in that the barium titanium oxide and the zeolitic, crystalline aluminosilicate are collectively incorporated in a matrix. 3 A fluidizable cracking catalyst composition according to claim 1 or 2, characterized in that the catalyst contains 1 to 20 per cent by weight of barium titanium oxide. 4 A fluidizable cracking catalyst composition according to claim 1, characterized in that the barium titanium oxide is physically separated from the zeolitic, crystalline aluminosilicate by composing the catalyst of a. catalytically active particles comprising a zeolitic, crystalline aluminosilicate embedded in matrix material, and b. catalytically less active particles comprising barium titanium oxide embedded in matrix material. 5 A fluidizable cracking catalyst composition according to claim 4, characterized in that the catalytically less active particles contain 10-40 per cent by weight of barium titanium oxide. 6 A fluidizable cracking catalyst composition according to any one of the predecing claims, characterized in that the barium titanium oxide used is barium titanate. 7 Particles comprising barium titanium oxide embedded in a matrix material. 8 Particles according to claim 7, characterized in that the barium titanium oxide used is barium titanate. 9 A process for cracking metal-containing feedstocks by using a cracking catalyst composition, characterized in that use is made of a cracking catalyst composition according to any one of the claims 1 to 5. 10 A process according to claim 9 in which use is made of a cracking catalyst composed of: a. catalytically active particles comprising a zeolitic, crystalline aluminosilicate embedded in matrix material, and b. catalytically less active particles comprising a barium titanium oxide embedded in matrix material, the metal-containing feedstock first being brought into contact with the catalytically less active particles and subsequently with the catalytically active particles. 11 A process according to claim 9 or 10, characterized in that the barium titanium oxide used is barium titanate.

Inventors: GROENENBOOM, CORNELIS JACOBUS
Applicants: AKZO N.V.
Application year: 1986
Main classification: C10G11
IPC codes: C10G11, B01J37, B01J29