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Low carbon alkane dehydrogenation catalyst and preparation method thereof

A catalyst and propane dehydrogenation technology, which is applied in the direction of hydrocarbons, hydrocarbons, chemical instruments and methods, etc., can solve problems such as complexity and low commercial application potential, and achieve simple preparation methods, avoid active component aggregation, The effect of mature technology

Active Publication Date: 2016-06-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the prior art, the method for improving the dispersion of active components in Pt-based catalysts is relatively complicated and has little potential for commercial application

Method used

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  • Low carbon alkane dehydrogenation catalyst and preparation method thereof
  • Low carbon alkane dehydrogenation catalyst and preparation method thereof

Examples

Experimental program
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Effect test

example 1

[0016] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 30g, deionized water was added dropwise to initial moistening, and the volume of consumed water was 27mL. Assuming that the Pt content accounts for 0.3wt% of the catalyst, weigh 0.09g of Pt-containing chloroplatinic acid and dissolve it in deionized water, set the volume to 27mL, add it to the above sample, age for 4h, dry at 80°C for 8h, and roast at 600°C for 4h . The sample obtained in the above steps is placed in a tubular heating furnace, heated to 400°C under a nitrogen atmosphere, and a mixed gas of methane, nitrogen, and oxygen is introduced, wherein the methane concentration is 15v%, the oxygen concentration is 3v%, and the volume space velocity of the mixed gas is 800h -1 , keep the temperature for 1h, after the end of the constant temperature, it will be cooled to...

example 2

[0019] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 30g, deionized water was added dropwise to initial moistening, and the volume of consumed water was 27mL. Assuming that the Pt content accounts for 0.2wt% of the catalyst, weigh 0.06g of Pt-containing chloroplatinic acid and dissolve it in deionized water, set the volume to 27mL, add it to the above sample, age for 2h, dry at 120°C for 4h, and roast at 500°C for 8h . The sample obtained in the above steps is placed in a tubular heating furnace, heated to 450°C under a nitrogen atmosphere, and a mixed gas of methane, nitrogen, and oxygen is introduced, wherein the concentration of methane is 10v%, the concentration of oxygen is 1v%, and the volumetric space velocity of the mixed gas is 1000h -1 , keep the temperature for 0.5h, after the end of the constant temperature, it wil...

example 3

[0021] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 30g, deionized water was added dropwise to initial moistening, and the volume of consumed water was 27mL. Based on the fact that the Pt content accounts for 0.4wt% of the catalyst, weigh 0.12g of Pt-containing chloroplatinic acid and dissolve it in deionized water, set the volume to 27mL, add it to the above sample, age for 8h, dry at 100°C for 6h, and roast at 700°C for 4h . The sample obtained in the above steps is placed in a tubular heating furnace, heated to 350°C under a nitrogen atmosphere, and a mixed gas of methane, nitrogen, and oxygen is introduced, wherein the concentration of methane is 20v%, the concentration of oxygen is 5v%, and the volume space velocity of the mixed gas is 500h -1 , keep the temperature for 2h, after the end of the constant temperature, it w...

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Abstract

The invention discloses a preparation method of a propane dehydrogenation catalyst. The method comprises the processes of: taking Sn-containing alumina as a carrier, firstly loading active component Pt, performing drying and roasting, then employing a mixed gas containing oxygen and methane to conduct dechlorination treatment on the carrier for 0.5h-4h at 300DEG C-500DEG C, preferably 350-450DEG C, controlling the space velocity of the mixed gas at 200h<-1>-2000h<-1>, the methane concentration of the mixed gas at 5v%-30v%, and the oxygen concentration at 0.5v%-10v%, and leaving the balance inert gas; and finally loading an assistant K, and then carrying out drying and roasting to obtain the propane dehydrogenation catalyst. The method can effectively remove chlorine from the catalyst without hydro-thermal treatment, significantly improves the activity stability of the catalyst and reduces the active metal dosage, and the preparation method is simple.

Description

technical field [0001] The invention relates to a low-carbon alkane dehydrogenation catalyst and a preparation method thereof, in particular to a propane dehydrogenation propylene catalyst and a preparation method thereof. Background technique [0002] The development and application of shale gas in North America has led to a sharp drop in the price of natural gas relative to crude oil prices. At the same time, it has also made the raw materials of ethylene crackers lighter, resulting in a sharp drop in the production of propylene, a by-product of petroleum as raw materials. Moreover, with the increasing scarcity of petroleum resources, the production of propylene has changed from relying solely on petroleum as a raw material to diversifying the technical route of raw material sources, which has gradually become a trend. Dehydrogenation of propane by-produced in natural gas (conventional natural gas, shale gas, coal bed methane, combustible ice, etc.) to produce propylene is...

Claims

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Application Information

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IPC IPC(8): B01J23/62C07C5/333C07C11/06
CPCY02P20/52
Inventor 张海娟李江红王振宇乔凯
Owner CHINA PETROLEUM & CHEM CORP