SYNTHETIC EXPANDED LAYERED MINERALS AND PROCESS FOR PRODUCING THEM

Abstract: Compositions conforming to the formula Ax ⁺⁺By ⁺⁺⁺(OH) 2x+3y-nz D z h- tH₂O wherein A is a divalent metal, B is a trivalent metal, D is a polyanion, x,y,z and t are numbers greater than zero and n is a whole number preferably from 1 to 10 and the ratio of x:y is equal to or greater than 0.5 and less than or equal to 10 and a method for preparing said compositions are described.

Description: This invention relates to a new class of synthetic minerals and particularly pertains to expanded layered minerals which have been exchanged with polyanions and to methods for preparing them. The pillaring of clay such as montmorillonite or bentonite by certain cationic clusters in order to produce an expanded interlaminar region useful for heavy oil cracking is described in U.S. Patents Nos. 4,238,364 and 4,248,739, for instance. A discussion of the differences between molecular seives (cage-like), which are also known as zeolites, when compared with cross-linked smectites (montmorillonite, hectorite, and synthetic fluorhectorites which are ion-exchanged with small globular cations, e.g., tetramethyl ammonium and ethylene diammonium ions) appears in an article by Shabtai, in La Chimica e L'industria , v . 61 , n. 10., October 1979. The exchange of some small anions with double layer structures having brucite-like layer ions is described by Allman in Chimia , 24 , 99(1970) and the exchange of hydrotalcite [Mg₆Al₂(OH)₁₆·CO₃·4H₂O] with anions such as Cl⁻, NO₃⁻, CO₃⁻⁻, oxalic acid and salicylic acid is described in Clay and Clay Minerals , 26 , 441(1978); 28 , 50(1980) and in Clay Minerals , 7 , 193(1967). US-A 3 879 523 relates to a composite metal hydroxide expressed by the following composition formula: M x ²⁺ M y ³⁺ (OH) 2x+3y-2z (A²⁻) z aH₂O such composite metal hydroxide having a layer crystal structure and exhibiting an endothermal peak owing to isolation of crystal water at a temperature exceeding 200°C, differential thermal analysis. Much of the prior art relates to layered silicates which are cation exchanged. The use of layered silicates greatly limits the variety of materials possible in the smectic framework and cation exchange limits to a significant degree the kind of elements which can be used in the exchange reaction with the smectic backbone structure. Workers who have used other than layered silicates have failed to utilize the expandable nature of these materials by exchanging them with large polyanion cluster materials. I have discovered a new class of compounds which are the products of anion exchange reactions between certain layered (smectic) minerals and large metal cluster anions also called polyanions wherein the smectic mineral conforms to the formula A x ⁺⁺B y ⁺⁺⁺(OH) 2x+3y-nz C z n- ·tH₂O wherein A is a divalent metal, B is a trivalent metal, C is an anion such as NO₃⁻, Cl,⁻ ClO₄⁻, CO₃⁻⁻, etc., x, y, z and t are numbers greater than zero, n is a whole number preferably from 1-10 and the ratio x:y is equal to or greater than 0.5 and less than or equal to 10; and wherein the large metal cluster anion is a polyanion which is composed of metal and/or non-metal atoms arranged in a network having a net negative charge. I have also discovered a process for making this new class of compounds. The new compounds of my invention are useful in ion-exchange reactions and they can be used as catalysts for the combustion of hydrocarbons and/or other air pollutants such as sulfur oxides and nitrogen oxides. Because of their high surface area (which can vary from 5 to 250 M²/g, BET, or higher and preferably from 30 to 250 M²/g) and large variety of components and what is believed to be a layered structure, the compounds of my invention are also useful catalysts for hydrocarbon conversion processes such as hydrodesulfurization, denitrification, catalytic cracking, hydrocracking, and the like. The preferred layered or smectic materials for use as substrates in the preparation of the compounds embodied in my invention are those conforming to the formula A x ⁺⁺B y ⁺⁺⁺(OH) 2x+3y-nz C z n- ·tH₂O wherein A is at least one member selected from the group consisting of copper, calcium, zinc, cobalt, iron, cadmium, mercury, lead, manganese, magnesium, tin, strontium, barium, nickel, platinum and palladium; B is at least one member selected from the group consisting of aluminum, iron, antimony, indium, chromium, cobalt, lanthanum and the other rare earths, ruthenium, rhodium, and bismuth; and C is an anion such as NO₃⁻, Cl⁻, CO₃²⁻, SO₄⁻⁻ etc., and x,y,z,n and t have the earlier mentioned designations. The polyanion for exchange with the smectic material is at least one selected from the group consisting of Ta₆O₁₈OH⁻⁷, Nb₆O₁₈OH⁻⁷, V₁₀O₂₈⁻⁶, PMo₆V₆O₄₀⁻³, PMo₆W₆O₄₀⁻³, P₃O₁₀⁻⁵,PMo₁₂O₄₀⁻³, Mo₇O₂₄⁻⁶, NiW₆O₂₄H₆⁻⁴, As₂Mo₁₈O₆₂⁻⁶, TeMo₆O₂₄⁻⁶, PMo₁₀V₂O₄₀⁻⁵, CoW₁₂O₄₀⁻⁶, B₁₁C₂H₁₂ , Pt₁₈(CO)₃₆⁻², Rh₆(CO)₁₅⁻², Re₃Cl₁₂⁻³, Ni₃Cr₂(CO)₁₆⁻², H₃Ru₄(CO)₁₂⁻, HRe₃(CO)₁₂⁻², HFe₄(CO)₁₃⁻ and the like. A particularly preferred group of polyanions are the heteropoly anions including those discussed in the bulletin entitled "Heteropoly Compounds of Molybdenum and Tungsten", by George A. Tsigdinos, Climax Molybdenum Co., Bulletin Cdb-12a, Nov. 1969. See also Chemical And Engineering News , August 30, 1982, pp. 28-41 and Topics in Current Chemistry , Vol. 76 , pp 1-64, Springer-Verlag, 1978. In general, the smectic mineral material is prepared by slurrying or by a precipitation method. In the slurry procedure, for instance, the divalent metal (A) oxide in water and one-half the stoichiometric amount of trivalent metal (B) ion is added to the slurry. The slurry is then heated for a time, filtered and washed. The resulting solid is reslurried and the other half of the trivalent metal ion is added to the slurry which is also heated, filtered and washed followed by drying. The exchange reaction is carried out by slurrying the smectic mineral material in water or a non-aqueous solvent which contains the dissolved metal cluster polyanion. The exchange procedure can be done in more than one step if desired. The polyanion exchanged smectic materials of this invention are useful per se or they may be calcined before use as catalysts for the oxidation of methane, sulfur oxides, nitrogen oxides, etc., preferably at a temperature in the range of from 100° to 1000°C. and preferably from about 300° to about 600°C. in air, other oxygen containing gases or in an inert, oxygen free atmosphere such as in nitrogen or in a reducing atmosphere such as hydrogen for from a few minutes to several hours or more. The compositions and process of this invention are further illustrated in the following examples. EXAMPLE 1 A slurry of 90 g. of zinc oxide was prepared in 50 g. of deionized water. To this slurry was added 308 ml of 1 M solution of Al(NO₃)₃·6H₂O in water and the pH was adjusted with water to 3.6-4.0. The slurry was heated with stirring for six hours at 90°C. The solid was isolated by filtration and was washed with deionized water. The solid was then reslurried in 100 g. of deionized water and 308 ml of 1 M solution of Al(NO₃)₃·6H₂O in water was added to the slurry. Again the pH of the slurry was adjusted to 3.6 to 4.0 with water and the slurry was maintained at 90°C. overnight. The resulting very thick slurry was then filtered and washed thoroughly with deionized water and the solid was dried at 110-120°C. overnight. The X-Ray diffraction analysis of this solid showed a pattern consistent with the hydrotalcite type of layered mineral Zn x Al y (OH) 2x+3y-nz ·z(NO₃)·tH₂O. EXAMPLE 2 A slurry of 90 g. of zinc oxide in 50 g. of water was prepared and to this was added 308 ml of 1 M solution of Cr(NO₃)₃·9H₂O. The pH of the mixture was between 3.6 and 4.0. This mixture was heated at 90°C. with stirring for six hours. The resulting purple solid was collected by filtration and was washed thoroughly with deionized water. The solid was then reslurried in 100 g. of water. To this slurry was added 380 ml of 1 M chromium nitrate solution and the pH was adjusted to 3.6-4.0 with water. This mixture was stirred for six hours at 90°C and the solid was collected by filtration and was washed with large amounts of water. The resulting solid was dried overnight at 110-120°C. The X-Ray diffraction pattern of the dried solid was found to agree with a layered material of the form Zn x Cr y (OH) 2x+3y-nz ·z(NO₃)·tH₂O. EXAMPLE 3 A solution was prepared by dissolving 247.6 g. of Al(NO₃)₃·9H₂O and 366.7 g. of Zn(NO₃)₂·H₂O (30.8% H₂O) in enough water to make 2 l. of solution. A second solution of 160 g. of NaOH in enough water to make 2 l. of solution was also prepared. The two solutions were then mixed by dropwise addition of both to a container and the addition was done in such a manner than the pH of the resulting mixture was maintained at about 10. The resulting white solid material in the mixture was isolated by filtration, was washed with large amounts of water and was dried overnight at 110°-120°. The dried solid was ground and reslurried in 500 g. of water to remove traces of NaNO₃. The slurry was stirred at 30°C. for an hour and the solid was then collected by filtration and was washed with water and dried overnight at 110°-120°C. X-Ray diffraction analysis of this solid showed a hydrotalcite type material, Zn x Al y (OH) 2x+3y-nz ·z(NO₃)·tH₂O. EXAMPLE 4 A 2 molar solution of NaOH in water and a solution of 0.67 molar Zn(NO₃)₂ and 0.33 molar Cr(NO₃)₃ were prepared as in Example 3. The two solutions were mixed as in Example 3 in such a manner as to maintain the pH of the resulting mixture at about 10. The resulting purple solid was collected by filtration and was washed with large amounts of water. The solid was dried overnight at 110°-120°C. The dried solid was ground, reslurried in 500 g. of water and stirred at 30°C for two hours. The solid was then collected by filtration, washed with a large amount of water and dried overnight at 110°-120°C. The X-Ray diffraction pattern of the dried solid showed it to have a hydrotalcite structure Zn x Cr y (OH) 2x+3y-nz ·z(NO₃)·tH₂O. EXAMPLE 5 15 g. of the material prepared in Example 1 was slurried in 100 ml of an aqueous solution containing 10 g. of 12-heteropoly phosphomolybdic acid. The exchange was carried out for 45 minutes at 80°-90°C. and the yellow solution became colorless during that time. The resulting yellow solid was collected by filtration, was washed with large increments of water and was resubjected to the same exchange procedure described above once again. The final yellow solid was dried at 110°-120°C. overnight. The dried solid was calcined in air at 300°C. for two hours. A sample of the material prepared according to the procedure of Example 1 which had not undergone the exchange reaction was also calcined at 300°C for two hours. The two calcined materials were then analyzed for surface area and chemisorptive properties. The material which had been exchanged with the 12-heteropoly phosphomolybdic acid showed a BET surface area of 89.2 M²/g. and showed a N₂ absorption of 40 mg/g. of absorbent and a neopentane absorbance of 30 mg/g. of absorbent. On the other hand, the calcined, non-exchanged hydrotalcite material showed a BET surface area of less than 1 M²/g. and no significant absorption of either N₂ or neopentane. EXAMPLE 6 A 15 g. sample of the material prepared in Example 2 was subjected to the same exchange procedure described in Example 5. The exchanged material was calcined at 300°C. for two hours and similarly a sample of the unexchanged material from Example 2 was also calcined in the same way. The calcined, exchanged material was found to have a BET surface area of 69.1 M²/g. and typical Langmuir isotherms of 24 mg/g. of N₂ and 20 mg/g. of neopentane per gram of absorbent whereas the calcined, unexchanged hydrotalcite material had a BET surface area of less than 1 M²/g. and showed no appreciable absorption. EXAMPLE 7 A slurry of 30g. of NH₄VO₃ in 100 ml of water was stirred at 50°-60°C. overnight. The solid was separated by filtration and the remaining yellow solution was slurried with 20 g. of the solid prepared in Example 1. (The yellow solution had a pH of about 5 and contained V₁₀O₂₈⁶⁻ ions.) The slurry was stirred at 90°C. for one hour and the resulting yellow solid was collected by filtration, was washed with water and exchanged as above twice more. The final solid product was dried overnight at 110°-120°C. and then was calcined at 300°C. for two hours. The resulting solid was found to have a BET surface area of 169.2 M²/g. EXAMPLE 8 A mixture of 4 g. of Nb₂O₅ and 3 g. of KOH was heated overnight in a platinum crucible at 600°C. The cooled solid was stirred in 50 g. of water for 30 minutes and the mixture was filtered. The solid was discarded and the filtrate was heated at reduced pressure to remove water. The remaining solid was dissolved in about 5-8 g. of water and to the resulting clear solution was added 20 g. of absolute ethanol. The white precipitate which formed was isolated by filtration and was dried. The dried material was found by analysis to be K₇Nb₆O₁₈OH. A solution of 5.5 g. of the material described just above was prepared in 100 ml of water and to this solution was added 20 g. of the material prepared according to Example 1. The resulting slurry was heated to 95°C. and stirred at this temperature for one hour. The resulting purple solid was collected by filtration and was washed with large amounts of water. The solid was dried at 110°-120°C. overnight. After calcining at 300°C for two hours the solid exhibited a BET surface area of 108.4 M²/g. EXAMPLE 9 A slurry was prepared from 12 g. of the material prepared according to Example 4, 7 g. of 12-heteropoly phosphomolybdic acid and 50 ml of water. The slurry was stirred for thirty minutes at 90°C. and the resulting green insoluble solid was collected by filtration and was washed with a large excess of water. The exchange procedure described just above was repeated on the green solid twice more and the final solid product was washed, dried and calcined at 300°C. for two hours. EXAMPLE 10 A mixture of 5 g. of zinc oxide, 12 g. of 12-heteropoly phosphomolybdic acid and 6.8 g. of Cr(NO₃)₃·9H₂O in 50 ml of water was stirred at 100°C. until the water had evaporated. The residual solid was then dried overnight at 110-120°C and finally was calcined at 300°C for two hours. This material, which is outside the scope of this invention was found to have a BET surface area of 5 M²/g. This material was made for the purpose of comparison with the materials embodied in this invention. EXAMPLE 11 A mixture which was made up of 5 g. of ZnO, 12 g. of 12 heteropoly phosphomolybdic acid and 6.8 g. of Cr(NO₃)₃·9H₂O and 50 ml of water was stirred at 80°C. for an hour, the solid was isolated, washed and calcined as in Example 10. The final solid which is outside the scope of this invention was found by analysis to have a BET surface area of 7.9 M²/g. EXAMPLE 12 Materials described in Examples 2, 4, 6, 9, 10 and 11 were tested in the form of 12-20 mesh particles as catalysts for the oxidation of methane. Each of the catalysts (3.3 g.) which had been calcined in air at 300°C for two hours was first diluted with from 3-10 g. of quartz chips (12-20 mesh) and the oxidation reactions were run in a small fixed bed tube reactor at ambient pressure. The feed to the reactor was a mixture of 80% by volume air and 20% methane and in each case the weight hourly space velocity was about 10 hr⁻¹. Effluent gases from the reactor (methane, CO₂ and CO) were analyzed by gas chromatograph and the conversion of methane to carbon oxides are given in the Table I. Catalyst from Example Reaction Temp.°C. % CH₄ Conversion 2 580 Less than 1 4 580 Less than 1 6 580 18.3 9 580 16.68 10 580 Less than 1 11 580 Less than 1 EXAMPLE 13 Some of the material prepared according to Example 2 (12 g.) was slurried in a solution of 7.0 g. of 12-heteropoly phosphomolybdic acid in methanol and the slurry was stirred and heated at 55°C. for one-half hour. During this time the solution became colorless. The resulting insoluble solid was collected by filtration and was washed with 100 ml of methanol. The solid product was reslurried in a solution of 12.0 g. of the heteropoly acid in methanol and the slurry was stirred at 60°C. for two and one-half hours. The solid was collected by filtration, washed with 100 ml of methanol and a large amount of water and was dried at 110°C. EXAMPLE 14 The procedure of Example 13 was followed using the materials described in Example 4. EXAMPLE 15 In accordance with the procedures of Examples 1 and 3 a number of hydrotalcite-like smectic materials were prepared and in some cases the surface area was determined by the BET method after calcination at 300°C. The materials prepared and results obtained are shown in Table 2. EXAMPLE 17 Several hydrotalcite like materials of the type described in Example 16 and Table 2 were exchanged with polyanions by procedures given in Example 3. The calcined exchanged materials which are embodied in this invention were found to have high surface areas (BET) in all cases in which surface area was determined. The materials used and results obtained are given in Table 3. A B D Surface Area, M²/g. Zn Al Ta₆O₁₈(OH)⁻⁷ 140.6 Zn Al Nb₆O₁₈(OH)⁻⁷ 95.0 Zn Al V₁₀O₂₈⁻⁶ 169.2 Zn Al PMo₁₂O₄₀⁻³ 89.2 Zn Al PW₁₂O₄₀⁻³ 85.4 Zn Al PMo₆W₆O₄₀⁻³ 91.0 Zn Al PMo₆V₆O₄₀⁻⁵ 78.2 Zn Al Mo₇O₂₄⁻⁶ -- Zn Cr Ta₆O₁₈(OH)⁻⁷ 122.3 Zn Cr Nb₆O₁₈(OH)⁻⁷ 108.4 Zn Cr PMo₆W₆O₄⁻³ 80 Zn Cr PMo₆V₆O₄₀⁻⁵ 115 Zn Cr Mo₇O₂₄⁻⁶ -- Zn Cr PMo₁₂O₄₀⁻³ 69.1 Mg Al Mo₇O₂₄⁻⁶ 71.5 Mg Al PMo₆V₆O₄₀⁻⁵ 92.2 Mg Al V₁₀O₂₈⁻⁶ -- Cd Al PMo₁₂O₄₀⁻³ 85 Cu Al V₁₀O₂₈⁻⁶ -- Cu Al Mo₇O₂₄⁻⁶ -- Cu Cr V₁₀O₂₈⁻⁶ -- Cu Cr Mo₇O₂₄⁻⁶ -- Co Al PMo₆V₆O₄₀⁻⁵ 48 Co Al V₁₀O₂₈⁻⁶ -- Co Al Mo₇O₂₄⁻⁶ -- Ca Al PMo₆V₆O₄₀⁻⁵ 133 Mn Al V₁₀O₂₈⁻⁶ -- Mn Al Mo₇O₂₄⁻⁶ -- Ni Al V₁₀O₂₈⁻⁶ -- Ni Al Mo₇O₂₄⁻⁶ --

Claims: The composition conforming to the formula A x ⁺⁺B y ⁺⁺⁺(OH) 2x+3y-nz D z n- ·tH₂O wherein A is a divalent metal, B is a trivalent metal, D is at least one polyanion, selected from the group consisting of Ta₆O₁₈OH⁻⁷, Nb₆O₁₈OH⁻⁷, V₁₀O₂₈⁻⁶, PMo₆V₆O₄₀⁻³, PMo₆W₆O₄₀⁻³, P₃O₁₀⁻⁵, PMo₁₂O₄₀⁻³, Mo₇O₂₄⁻⁶, NiW₆O₂₄H₆⁻⁴, As₂Mo₁₈O₆₂⁻⁶, TeMo₆O₂₄⁻⁶, PMo₁₀V₂O₄₀⁻⁵, CoW₁₂O₄₀⁻⁶, Pt₁₈(CO)₃₆⁻², Rh₆(CO)₁₅⁻², Re₃Cl₁₂⁻³, Ni₃Cr(CO)₁₆⁻², H₃Ru₄(CO)₁₂⁻, HRe₃(CO)₁₂⁻² and HFe₄(CO)₁₃⁻³, x, y, z and t are numbers greater than zero, and n is a whole number preferably from 1 to 10 and the ratio of x:y is equal to or greater than 0.5 and less than or equal to 10. The composition of Claim 1 wherein A is at least one member selected from the group consisting of copper, calcium, zinc, cobalt, iron, cadmium, mercury, lead, manganese, magnesium, tin, strontium, barium, nickel, platinum and palladium. The composition of Claim 2 wherein B is at least one member selected from the group consisting of aluminum, iron, antimony, indium, chromium, cobalt, lanthanum and other rare earths, ruthenium, rhodium and bismuth. The composition of Claim 3 wherein A is zinc, B is aluminum and D is PMo₁₂O₄₀⁻³. The composition of Claim 3 wherein A is zinc, B is chromium and D is PMo₁₂O₄₀⁻³. The composition of claim 3 wherein A is zinc, B is aluminum and D is V₁₀O₂₈⁻⁶. The composition of claim 3 wherein A is nickel, B is aluminum and D is Mo₇O₂₄⁻⁶. The composition of claim 3 wherein A is zinc, B is bismuth and D is Mo₇O₂₄⁻⁶. The composition of claim 3 wherein A is zinc, B is aluminum and D is CoW₁₂O₄₀⁻⁶. The composition of claim 3 wherein A is copper, B is chromium and D is V₁₀O₂₈⁻⁶. The composition of claim 3 wherein A is calcium, B is aluminum and D is PMo₆V₆O₄₀⁻⁵. The process for preparing the composition conforming to the formula A x ⁺⁺B y ⁺⁺⁺(OH) 2x+3y-nz D z n- · tH₂O wherein A is a divalent metal, B is a trivalent metal, D is at least one polyanion selected from the group consisting of Ta₆O₁₈OH⁻⁷, Nb₆O₁₈OH⁻⁷, V₁₀O₂₈⁻⁶, PMo₆V₆O₄₀⁻³, PMo₆W₆O₄₀⁻³, P₃O₁₀⁻⁵, PMo₁₂O₄₀⁻³, Mo₇O₂₄⁻⁶, NiW₆O₂₄H₆⁻⁴, As₂Mo₁₈O₆₂⁻⁶, TeMo₆O₂₄⁻⁶, PMo₁₂O₄₀⁻⁵, CoW₁₂O₄₀⁻⁶, Pt₁₈(CO)₃₆⁻², Rh₆(CO)₁₅⁻², Re₃Cl₁₂⁻³, Ni₃Cr(CO)₁₆⁻², H₃Ru₄(CO)₁₂⁻, HRe₃(CO)₁₂⁻² and HFe₄(CO)₁₃⁻³, x, y, z and t are numbers greater than zero, and n is a whole number preferably of from 1 to 10 and the ratio of x:y is equal to or greater than 0.5 and less than or equal to 10 comprising slurrying a smectic material conforming to the formula A x ⁺⁺B y ⁺⁺⁺(OH) 2x+3y-nz C z n- ·tH₂O wherein A, B, x, y, z, n and t have the foregoing designations and C is at least one anion selected from the group consisting of NO₃⁻, Cl⁻, CO₃⁻² and SO₄⁻² in water or a non-aqueous solvent which contains the dissolved polyanion and recovering the solid product. The process of Claim 12 wherein A is at least one member selected from the group consisting of copper, calcium, zinc, cobalt, iron, cadmium, mercury, lead, manganese, magnesium, tin, strontium, barium, nickel, platinum and palladium. The process of Claim 13 wherein B is at least one member selected from the group consisting of aluminum, iron, antimony, indium, chromium, cobalt, lanthanum and other rare earths, ruthenium, rhodium and bismuth. The process of Claim 14 wherein A is zinc, B is aluminum and D is PMo₁₂O₄₀⁻³. The process of Claim 14 wherein A is zinc, B is chromium and D is PMo₁₂O₄₀⁻³. The process of Claim 14 wherein A is zinc, B is aluminum and D is V₁₀O₂₈⁻⁶. The process of Claim 14 wherein A is nickel, B is aluminum and D is Mo₇O₂₄⁻⁶.

Inventors: WOLTERMANN, GERALD MARTIN
Applicants: ASHLAND OIL, INC.
Application year: 1984
Main classification: C01F5
IPC codes: C01G33, B01J27, B01J23, B01J21, C01G9, B01J29, C01G15, C01G39, C01G37, B01J41, C01B13, C01G31, C01B25, C01G53