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Catalyst for hydrogen selective combustion reaction and preparation method thereof

A combustion reaction and catalyst technology, applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of high loss rate of raw materials, short catalyst life, etc. high sex effect

Active Publication Date: 2013-04-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] One of the technical problems to be solved by the present invention is the problem of short catalyst life and high loss rate of raw materials in the prior art in the hydrogen selective combustion reaction, and a catalyst for the hydrogen selective combustion reaction is provided

Method used

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  • Catalyst for hydrogen selective combustion reaction and preparation method thereof
  • Catalyst for hydrogen selective combustion reaction and preparation method thereof
  • Catalyst for hydrogen selective combustion reaction and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] A certain amount of dry powder pseudo-boehmite, alumina trihydrate (ratio 30:70) and 5% of the total weight of aluminum oxide are loaded into the rolling ball machine, and the rolling machine is started, and 2% (weight) is sprayed. The dilute nitric acid binder, stirring continuously to fully mix the dry powder and water, when the binder spraying ends, the alumina material rolls into a particle cluster with a diameter of 1-2mm, and then continuously and evenly sprinkles the dry powder and binder, Make the particles reach 4mm. Vacuum drying at 80°C for 24 hours, air drying at 300°C for 2 hours, and calcination in an oxygen atmosphere at 1200°C for 10 hours to make spherical α-Al 2 o 3 carrier.

[0020] 40 grams of 15% alumina sol, 60 grams of 2% glycerin solution, and 0.3 grams of Span 80 were made into slurry. Then add 0.6 grams of potassium feldspar and 40 grams of γ-Al with a particle size of 20 microns or less to this mixture. 2 o 3 powder (specific surface area...

Embodiment 2

[0023] Add aluminum oxide, silica sol, and magnesium oxide into the kneader according to the ratio, mix evenly, then add dilute nitric acid with a concentration of 2% (weight), knead to form a lump material, extrude into strips and press balls, and dry in the air at 100°C 4 hours, 300 DEG C in air for 4 hours, and 1400 DEG C in air for 2 hours to make a spherical cordierite carrier with a diameter of 3 mm.

[0024] SnCl 2 dissolved in water, and the above solution was impregnated in θ-Al 2 o 3 (solid-to-liquid ratio 1:2) powder, dried at 150°C for 2 hours, calcined at 400°C for 4 hours, and then pulverized to below 15 microns. 40 grams of 15% alumina sol, 60 grams of 3% polyacrylamide solution, and 0.4 grams of nonylphenol ethoxylate-5 were made into slurry. Then add 0.3 g of calcium silicate, 40 g of θ-Al impregnated with Sn to this mixture 2 o 3 powder. After stirring for about ten minutes, 2.3 g of 25% KCl aqueous solution was added, and the resulting slurry was subje...

Embodiment 3

[0027] The preparation method of the cordierite carrier is the same as in Example 2.

[0028] 35 grams of 10% alumina sol, 60 grams of 4% cyclodextrin solution, and 1.0 gram of Tween-80 were slurried. After stirring for about ten minutes, add 0.52 g of 50% SnCl 4 solution, 0.4 grams of calcium silicate, 0.15 grams of barium oxide and 40 grams of δ-Al with a particle size of 20 microns or less 2 o 3 pink. The resulting slurry was ball milled for 4 hours at room temperature to control the particle size below 10 microns. The slurry was sprayed onto the cordierite carrier, dried at 80°C for 2 hours, then heated to 150°C and dried again for 2 hours, and finally calcined at 900°C for 8 hours to obtain a layered composite carrier.

[0029] Dissolve lithium nitrate and sodium chloroplatinite in water respectively to prepare a mixed solution, adjust the solution with HCl to make the pH value about 4, then heat the solution to 80°C, and impregnate the prepared layered composite carr...

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Abstract

The invention relates to a catalyst for hydrogen selective combustion reaction and a preparation method thereof, mainly solving the problems of short service life and high raw material loss rate of the catalysts in the prior art. The catalyst of the invention comprises a layered compound carrier consisting of an inner core of at least one inert carrier selected from alpha-Al2O3, dichroite, metal and carborundum, and at least one oxide porous coating material outer layer combined on the inner core and selected from gamma-Al2O3, Delta-Al2O3, Eta-Al2O3, Theta-Al2O3, silicon oxide, titanium oxideor zirconia; at least one noble metal selected from metallic ruthenium, rhodium, palladium, osmium, iridium and platinum, at least one modifying agent selected from alkali metals and alkaline-earth metals and at least one catalyst promoter selected from IVA compounds are loaded on the outer layer of the layered compound carrier. The problems are perfectly solved through the technical scheme of the catalyst and the preparation method thereof, and the catalyst can be used in the industrial production of hydrogen selective combustion reaction in the process of production of unsaturated hydrocarbon compounds by dehydrogenating saturated hydrocarbon compounds.

Description

technical field [0001] The invention relates to a catalyst for hydrogen selective combustion reaction and a preparation method thereof. Background technique [0002] The dehydrogenation of saturated hydrocarbons to produce unsaturated hydrocarbons is a relatively mature process. The classic process is that saturated hydrocarbons pass through a dehydrogenation catalyst under dehydrogenation conditions to obtain a mixture of dehydrogenated products and undehydrogenated reactants. Usually, the dehydrogenation reaction is carried out in the presence of water vapor. Dehydrogenation reaction, such as ethylbenzene dehydrogenation reaction, because the dehydrogenation reaction is an endothermic reaction, the bed temperature of the catalyst will decrease significantly during the reaction process, thereby resulting in a reduction in the conversion rate of raw materials. The reduction of the reaction temperature not only affects the equilibrium conversion rate of the reaction, but al...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/62B01J23/58B01J35/02B01J37/08B01J37/02B01J37/16C07C7/148C07C15/073B01J35/00
Inventor 李应成马春景缪长喜杨为民
Owner CHINA PETROLEUM & CHEM CORP