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Preparation method for light alkane dehydrogenation catalyst with non-uniformly distributed active components

A dehydrogenation catalyst, non-uniform distribution technology, applied in the field of catalysis, can solve the problems of insufficient stability and low selectivity of alkane dehydrogenation catalysts

Active Publication Date: 2014-01-01
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is to overcome the disadvantages of insufficient stability and low selectivity of the alkane dehydrogenation catalysts prepared in previous literatures, and provide a high activity, high selectivity and hydrothermal stability, long-term long life alkane dehydrogenation catalyst complex

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Weigh 65 grams of chromium trioxide, 5.5 grams of lanthanum nitrate, and 10 grams of sodium nitrate and dissolve them in 80 milliliters of water to obtain an impregnation solution. Take 30 grams of carbon powder and impregnate it with 20 milliliters of impregnation solution as a pre-treated pore-enlarging agent.

[0036] Weigh 250 grams of pseudo-boehmite powder of 80-100 microns, 50 grams of gibbsite powder of 50-100 microns, mix evenly with the pretreated pore-enlarging agent, and then add 200 ml of 10% nitric acid , Knead in a kneader to obtain a paste-like mass. The agglomerate was shaped on an extruder, then dried at 120°C for 6 hours, and calcined at 600°C for 4 hours to obtain a semi-finished catalyst.

[0037] Add 30 milliliters of water to the remaining impregnating liquid, impregnate the semi-finished catalyst with the impregnating liquid, then dry at 120°C for 6 hours, and roast at 760°C for 6 hours to obtain the finished dehydrogenation catalyst a1.

[003...

Embodiment 2

[0045] Weigh 65 grams of chromium trioxide, 6.2 grams of cerium nitrate, and 8 grams of potassium nitrate and dissolve them in 80 milliliters of water to obtain an impregnation solution. After mixing 20 grams of cellulose powder and 20 grams of wood powder, impregnate with 35 milliliters of soaking liquid as a pretreated pore-enlarging agent.

[0046] Weigh 260 grams of pseudo-boehmite powder with a particle size of 150-200 microns, 40 grams of γ-alumina powder with a particle size of 60-100 microns, mix them evenly with the pretreated pore-enlarging agent, and then add 20% nitric acid to the kneader 150 ml were kneaded to obtain a paste-like mass. The agglomerate was shaped on an extruder, then dried at 120°C for 4 hours, and calcined at 600°C for 5 hours to obtain a semi-finished catalyst.

[0047] Add 45 milliliters of water to the remaining impregnation liquid, impregnate the semi-finished catalyst with the impregnation liquid, then dry at 120°C for 6 hours, and roast at ...

Embodiment 3

[0050] Weigh 65 grams of chromium trioxide, 7.2 grams of zirconium oxynitrate, and 6.0 grams of magnesium nitrate and dissolve them in 80 milliliters of water to obtain an impregnation solution. After mixing 20 grams of carbon powder and 10 grams of scallop powder, impregnate with 30 milliliters of soaking liquid as a pretreated pore-enlarging agent.

[0051] Weigh 260 grams of amorphous aluminum hydroxide powder with a particle size of 70-100 microns, 40 grams of pyrenite powder with a particle size of 60-90 microns, mix them evenly with the pretreated pore-enlarging agent, and then add the remaining The dipping solution and 120 ml of 15% nitric acid were kneaded to obtain a paste-like mass. The agglomerate was formed on an extruder, then dried at 120°C for 6 hours, and calcined at 760°C for 8 hours to obtain the finished catalyst a3.

[0052] The propane dehydrogenation reaction performance test method of catalyst a3 is the same as the reaction performance test of catalyst ...

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Abstract

The invention discloses a preparation method for a light alkane dehydrogenation catalyst with non-uniformly distributed active components. The preparation method is characterized in that in the preparation process of the catalyst, through the addition of a pore-enlarging agent, the increase of catalyst pore volume and the change of the catalyst hole distribution, the catalytic reaction is facilitated better; meanwhile the active components are preloaded on the pore-enlarging agent, part or all active components are enabled to be relatively concentratedly distributed on the surfaces of part holes of the catalyst, the distribution of the active components on the inner surface of the catalyst is increased, and the active components are enabled be to distributed non-uniformly in the catalyst.

Description

technical field [0001] The invention relates to the technical field of catalysis, in particular to a method for preparing a low-carbon alkane dehydrogenation catalyst with non-uniform distribution of active components. Background technique [0002] With the rapid development of the chemical industry and the plastic products industry, the demand for low-carbon olefins has also increased rapidly. For example, the growth rate of demand for propylene as an organic chemical raw material has exceeded that of ethylene. It is a known method to produce low-carbon alkenes such as propylene and butene by dehydrogenating lower-carbon alkanes in the presence of a catalyst. Catalysts include noble metal catalysts using platinum and chromia / alumina catalysts with chromium as the main active component. Both of these catalysts require alkane dehydrogenation reaction at high temperature, which makes the catalyst activity easy to decrease. [0003] Using alumina as a carrier, supported chrom...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/26C07C11/06C07C5/333
CPCY02P20/52
Inventor 杨玉旺戴清高旭东孙彦民于海斌刘红光
Owner CNOOC TIANJIN CHEM RES & DESIGN INST