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A kind of catalyst for dehydrogenation of light alkane to olefin and its preparation method and use

A technology for alkane dehydrogenation and catalysts, which is applied in the direction of catalysts, carbon compound catalysts, chemical instruments and methods, etc. It can solve the problems of inconvenient regeneration of catalysts and achieve the effects of improving wear resistance and process performance

Active Publication Date: 2022-08-09
SOUTHWEST RES & DESIGN INST OF CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the fixed bed reactor, the catalyst is required to have a certain crushing strength to prevent the catalyst from being broken by impact during the filling process; the fixed bed reactor has the advantages of low investment and low design difficulty, but it is less effective for catalyst regeneration. Convenience, especially regeneration requires parking for refilling

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0034] The preparation method of this light paraffin dehydrogenation to olefin catalyst comprises the following steps:

[0035] S1, preparing a doped magnesia-aluminum spinel carrier;

[0036] The carrier is prepared by the sol-gel method + spray drying method:

[0037] A: Take a certain amount of pseudo-boehmite, add an appropriate amount of deionized water, and stir in a water bath at a certain temperature to obtain a uniform slurry A; the mass ratio of pseudo-boehmite to deionized water is (0.5-1) : (2-5), the temperature of water bath stirring is 50℃-80℃.

[0038] B: take by weighing an appropriate amount of magnesium nitrate, and add a small amount of auxiliary agent 1 and add deionized water to dissolve to obtain solution B;

[0039] C: Add the B solution to the A slurry evenly, add an appropriate amount of auxiliary agent II and stir evenly, dilute it with concentrated nitric acid and water with a volume ratio of 1:1 to form nitric acid, and then adjust it with nitric...

Embodiment 1

[0055] A kind of preparation method of light paraffin dehydrogenation to olefin catalyst, comprises the following steps:

[0056] S1, preparing a doped magnesia-aluminum spinel carrier;

[0057] A: Add an appropriate amount of deionized water to 0.2mol of pseudo-boehmite, and stir in a water bath at 65°C to obtain a uniform slurry A; the mass ratio of pseudo-boehmite to deionized water is 1:3.

[0058] B: Weigh 0.1mol of magnesium nitrate, and add 0.05mol of gallium nitrate to dissolve in deionized water to obtain solution B;

[0059] C: Add the B solution to the A slurry uniformly, add 0.002mol polyacrylamide and stir evenly, dilute with concentrated nitric acid and water by volume 1:1, then add it to adjust the gel, and adjust the pH value to be about 3;

[0060] D: The prepared gel is sprayed by the method of spray granulation to obtain a powdered carrier precursor, which is then calcined at 700°C for 4 hours as a carrier for use.

[0061] S2, sedimentation-precipitation ...

Embodiment 2

[0066] A kind of preparation method of light paraffin dehydrogenation to olefin catalyst, comprises the following steps:

[0067] S1, preparing a doped magnesia-aluminum spinel carrier;

[0068] A: Add an appropriate amount of deionized water to 0.2mol of pseudo-boehmite, and stir in a water bath at 65°C to obtain a uniform slurry A;

[0069] B: Weigh 0.1mol of magnesium sulfate, and add 0.05mol of gallium nitrate to dissolve in deionized water to obtain solution B;

[0070] C: Add the B solution to the A slurry uniformly, add 0.001mol melamine and stir evenly, dilute it with concentrated nitric acid at a volume ratio of 1:1, then add it to adjust the gel, and adjust the pH value to be about 4;

[0071] D: The prepared gel is sprayed by the method of spray granulation to obtain a powdered carrier precursor, which is then calcined at 700°C for 4 hours as a carrier for use.

[0072] S2, sedimentation-precipitation method to load Pt;

[0073] Disperse 10 g of the above carrier...

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PUM

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Abstract

The invention belongs to the technical field of catalyst preparation, in particular to a catalyst for producing olefins by dehydrogenation of light paraffins, a preparation method and uses thereof. The catalyst adopts modified spinel as the catalyst carrier, Pt as the main active component of the catalyst, and Sn, Zn, Ca, Ce, Mg, Nb, etc. as auxiliary components. , Improve the reaction activity and reaction selectivity, and have better performance than conventional catalysts and adapt to the use of fluidized beds.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, in particular to a catalyst for preparing olefins by dehydrogenation of light paraffins, and a preparation method and application thereof. Background technique [0002] The dehydrogenation of light alkanes (light alkanes, light alkenes, mainly including pure and / or mixed ethane, propane, butane and isobutane, etc.) to corresponding alkenes is an important and economical alkene production technology. [0003] Commercial dehydrogenation catalysts generally use supported catalysts with precious metal platinum as the active component, and a few use chromium-based catalysts. The catalyst support includes alumina (γ-Al 2 O 3 , mesoporous Al 2 O 3 etc.), molecular sieves (SAPO, HZSM-5, SBA-15, etc.), SiO 2 Wait. Catalytic reaction process technology includes Oleflex process (UOP company), Catofin process (ABB Lummus company) and STAR process (Krupp Uhdewcng company) and so on. [000...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/63C07C5/333C07C11/06
CPCB01J23/005B01J23/63C07C5/3337C07C2523/63C07C11/06Y02P20/52Y02P20/584
Inventor 艾珍梁衡潘相米李南锌李扬吴砚会韩伟
Owner SOUTHWEST RES & DESIGN INST OF CHEM IND