Catalyst used for preparing isobutene through isobutane dehydrogenation and preparation method and application thereof
A technology for producing isobutene and catalysts, which is applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problem of insufficient mechanical strength and high temperature stability, isobutane Deep dehydrogenation and cracking, poor dispersion of active components and other problems, to achieve the effect of inhibiting the formation of carbon deposits, high conversion rate of isobutane, and improving conversion rate of catalytic reaction
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Embodiment 1
[0039] This example provides a catalyst for producing isobutene by isobutane dehydrogenation. The catalyst uses magnesium aluminum spinel as a carrier, platinum nanoparticles as an active component, tin as a first auxiliary agent, and alkali metal potassium as a catalyst. The second auxiliary agent; its preparation process comprises the following steps:
[0040] Preparation of Magnesium Aluminum Spinel Support by Co-precipitation
[0041] Weigh 5.6354g Mg(NO 3 ) 2 ·6H 2 O and 8.2447g Al(NO 3 ) 3 9H 2 O, dissolve it in deionized water, stir and mix evenly, add dropwise ammonia water with a volume fraction of 50% to adjust the pH to 10, react to obtain a white colloid, filter, wash, dry at 120°C for 12 hours, and roast at 500°C for 4 Hours, a magnesium aluminum spinel carrier was obtained.
[0042] Preparation of Platinum Nanosol
[0043] The concentration of 8mL is 7.723×10 -3 mol / L of H 2 PtCl 6 The aqueous solution was fully mixed with 0.2252g stabilizer CTAB, and ...
Embodiment 2
[0050] This embodiment provides the application of the catalyst for isobutane dehydrogenation to isobutene obtained in Example 1 in isobutane dehydrogenation to isobutene, which includes the following steps:
[0051] The above-mentioned catalyst is reduced and activated in a hydrogen atmosphere, the reduction and activation temperature is 500 ° C, and the reduction and activation time is 2 hours;
[0052] The mixture of isobutane and hydrogen is used as the raw material, the molar ratio is 1:1, and the dehydrogenation reaction is carried out in the reactor. The operating conditions of the dehydrogenation reaction are as follows: the reaction temperature is 590°C, and the volume space velocity is 1350h -1 , The reaction pressure is normal pressure.
[0053] After the reaction, a gas chromatograph (model hp5830) was used to analyze the reaction tail gas online, the carrier gas was nitrogen, the detector was a hydrogen flame ionization detector, and a chromatographic workstation ...
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