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A kind of SIO2 modified low-carbon alkane dehydrogenation catalyst and preparation method thereof

A technology for dehydrogenation catalysts and low-carbon alkanes, which is applied in the direction of hydrocarbons, hydrocarbons, chemical instruments and methods, etc., can solve the problems of blocking secondary pores and changing the internal structure of pores, and achieves the improvement of mechanical strength and the selection of olefins. The effect of good resistance, high mechanical strength and wear resistance

Active Publication Date: 2018-12-04
SINOPEC DALIAN RES INST OF PETROLEUM & PETROCHEMICALS CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For mesoporous materials such as alumina, the pore size is larger, and silicon ester molecules can enter the pores of alumina, and the SiO remaining in the pores after calcination 2 It not only changes the internal structure of the pores, but also affects the loaded main catalytic components, and even blocks the secondary pores, so that the active components in the secondary pores cannot contact the reactants to carry out the catalytic reaction.

Method used

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  • A kind of SIO2 modified low-carbon alkane dehydrogenation catalyst and preparation method thereof

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Experimental program
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Effect test

Embodiment 1

[0033] (1) Select chromium nitrate as the active component precursor, weigh an appropriate amount of chromium nitrate and make it into an aqueous solution, impregnate 10kg of active Al 2 o 3 carrier, the immersion time is 5h. Then place it in a drying oven for drying, the drying temperature is 110° C., and the drying time is 6 hours. Then it is placed in a muffle furnace for calcination, the calcination temperature is 600°C, and the calcination time is 6h.

[0034] (2) Measure the mass water absorption rate of the catalyst obtained after roasting to 68%, prepare an aqueous solution with appropriate amount of copper nitrate and potassium nitrate with 7.11kg of ionized water, impregnate the catalyst obtained in step (1) to make it absorb water to saturation.

[0035] (3) Evenly spread the catalyst that has absorbed water to saturation on the drying belt with a thickness of 3.5cm. Control the transmission speed of the drying belt to 50m / h, the drying temperature to 150°C, and p...

Embodiment 2

[0048] (1) Select chromium acetate as the active component precursor, weigh an appropriate amount of chromium acetate and make it into an aqueous solution, impregnate 10kg of active Al 2 o 3 carrier, the immersion time is 6h. Then place it in a drying oven for drying, the drying temperature is 120° C., and the drying time is 5 hours. Then it is placed in a muffle furnace for calcination, the calcination temperature is 700°C, and the calcination time is 5h.

[0049] (2) Measure the mass water absorption rate of the catalyst obtained after roasting to 65%, and prepare an aqueous solution with an appropriate amount of cerium nitrate and ferric nitrate with 7.06 kg of ionized water, and impregnate the catalyst obtained in step (1) to make it absorb water to saturation.

[0050] (3) Spread the catalyst that has absorbed water to saturation evenly on the drying belt with a thickness of 4cm. Control the transmission speed of the drying belt to 45m / h, the drying temperature to 140°C...

Embodiment 3

[0055] (1) Select chromic acid as the precursor of the active component, weigh an appropriate amount of chromic acid and make it into an aqueous solution, impregnate 10kg of active Al 2 o 3 carrier, the immersion time is 6h. Then place it in a drying oven for drying, the drying temperature is 110° C., and the drying time is 5 hours. Then place it in a muffle furnace for calcination, the calcination temperature is 650°C, and the calcination time is 5h.

[0056] (2) Measure the mass water absorption rate of the catalyst obtained after roasting to 66%, prepare an aqueous solution with appropriate amounts of gallium nitrate and zinc nitrate with 7.49kg of ionized water, and impregnate the catalyst obtained in step (1) to make it absorb water to saturation.

[0057] (3) Spread the catalyst that has absorbed water to saturation evenly on the drying belt with a thickness of 4cm. Control the transmission speed of the drying belt to 45m / h, the drying temperature to 140°C, and pass th...

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Abstract

The invention discloses a SiO2 modified low carbon alkane dehydrogenation catalyst and a preparation method thereof. The external surface of the catalyst is a SiO2 coating, active Al2O3 is adopted as a carrier, chromium is adopted as an active component, one or more of K, Fe, Co, Ni, Zr, Ce, Cu, Zn, La and Ga is / are adopted as an assistant, and the catalyst comprises the SiO2 coating accounting for 0.05-1.0% of the weight of the carrier, the Cr2O3 accounting for 3.0-30.0% of the weight of the carrier, assistant metal(s) oxide accounting for 0.1-8.0% of the weight of the carrier, and the balance of alumina. The preparation method comprises the following steps: 1, loading the active component Cr to the active Al2O3 carrier, drying the active Al2O3 carrier loaded with Cr, and roasting the dried active Al2O3 carrier loaded with Cr; 2, carrying out saturated impregnation on the obtained roasted product in an impregnating solution containing assistant meta, and carrying out semidrying dehydration; 3, impregnating a catalyst precursor in an organic solvent solution containing estersil; and 4, drying the catalyst precursor, and roasting the dried catalyst precursor to obtain the catalyst. The catalyst has high mechanical strength and high wear resistance, and has good alkane conversion rate and good olefin selectivity in a low-carbon alkane dehydrogenation reaction.

Description

technical field [0001] The present invention relates to a SiO 2 A modified low-carbon alkane dehydrogenation catalyst and a preparation method thereof. Background technique [0002] The development of shale gas in North America has led to a sharp decline in natural gas prices relative to crude oil prices, while the production of large condensate liquids (NGLs) in shale gas has also increased rapidly. Shale gas condensate is rich in low-carbon alkanes such as ethane, propane, and butane. Ethane can be used as a cracking raw material to produce ethylene. Therefore, FCC technology alone cannot meet the rapidly growing demand for propylene. Dehydrogenation of low-carbon alkanes in natural gas (conventional natural gas, shale gas, coalbed methane, combustible ice, etc.) to produce low-carbon olefins is an effective way to solve this problem. Moreover, with the increasing scarcity of petroleum resources, the production of propylene has changed from relying solely on petroleum as...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/86B01J23/26C07C5/333C07C11/06
CPCY02P20/52
Inventor 王振宇郑步梅张淑梅
Owner SINOPEC DALIAN RES INST OF PETROLEUM & PETROCHEMICALS CO LTD
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