Bimetal reforming catalyst and preparation method thereof
A reforming catalyst and bimetallic technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of accelerating catalyst deactivation rate, reducing gasoline yield, increasing device operating costs, etc. , to achieve the effect of good stability, high liquid yield and low carbon deposition
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example 1
[0044] Catalysts described in the present invention are prepared.
[0045] (1) Preparation of Sn-containing spherical Al 2 o 3 carrier.
[0046] 100 grams of SB aluminum hydroxide powder (Germany, produced by Condea company) and an appropriate amount of deionized water are mixed to make the liquid / solid mass ratio 2.0, stirring and slurrying, adding 7.5 milliliters of dilute acid with a volume ratio of 1: 1, 30 The hydrochloric acid solution of the tin protochloride of gram urea and predetermined amount, make the Sn content in the solution be 0.30 mass % (relatively dry base aluminum oxide), stir 1 hour, add 30 gram kerosene and 3 gram fatty alcohol polyoxyethylene ethers Stir for 1 hour, and drop balls into the oleyl ammonia column to form. The wet bulb was solidified in ammonia water for 1 hour, then filtered, rinsed with deionized water for 2 to 3 times, dried at 60°C for 6 hours, dried at 120°C for 10 hours, and calcined at 600°C for 4 hours to obtain Sn-containing alum...
example 2
[0052] Catalyst is prepared by the method of example 1, difference is (2) the mass ratio of the citric acid contained in the impregnating liquid of step preparation and dry basis alumina is 8%, the composition of the catalyst B that makes is shown in Table 1, wherein platinum Radial distribution see figure 1 , the radial distribution of tin see image 3 .
[0053] The average concentration of Pt in the center area of catalyst B is 0.71, the average concentration of Pt in the spherical shell area is 0.40, and the ratio of the average Pt concentration in the spherical center area to the spherical shell area is 1.76.
example 3
[0061] Prepare catalyst by the method for example 1, difference is (2) step replaces citric acid with tartaric acid when preparing impregnation solution, the mass ratio of the tartaric acid contained in impregnation solution and dry base alumina is 7%, the composition of the prepared catalyst E See Table 1, where the radial distributions of platinum and tin are shown in figure 1 and image 3 .
[0062] The average concentration of Pt in the center area of catalyst E is 1.17, the average concentration of Pt in the spherical shell area is 0.54, and the ratio of the average Pt concentration in the spherical center area to the spherical shell area is 2.17.
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