Mixed C3/C4 alkane dehydrogenation catalyst and preparation method thereof

A dehydrogenation catalyst and catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem of low activity of mixed low-carbon alkanes dehydrogenation catalysts

Active Publication Date: 2014-10-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] One of the technical problems to be solved by the present invention is the low activity of mixed low-carbon alkane dehydrogenation catalysts in the prior art, and a new catalyst for mixed low-carbon alkane dehydrogenation is provided

Method used

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  • Mixed C3/C4 alkane dehydrogenation catalyst and preparation method thereof
  • Mixed C3/C4 alkane dehydrogenation catalyst and preparation method thereof
  • Mixed C3/C4 alkane dehydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Weigh 2 grams of SiO with a Si / Al ratio of 150 2 Carrier, add 10 ml of deionized water, pipette 0.18 ml of H 2 PtCl 6 solution, 1.80 ml of SnCl 4 solution, 3 mL NaNO 3 solution and 2.5 mL H 8 MON 2 o 4Solution, adjust the pH value of the solution to 1.5 with 2.5% ammonia water, then soak in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample in a muffle furnace at 550°C ℃ for 4 hours to obtain the desired catalyst. The mixed gas of propane and isobutane is adjusted by the mass flow meter, enters the preheating zone for mixing, and then enters the reaction zone. Both the preheating zone and the reaction zone of the reactor are heated by electric heating wires to make them reach the predetermined temperature. The stainless steel casing with an inner diameter of Ф9mm-Ф6mm and a length of about 400mm. After the reaction gas passes through the condensation tank, it enters the gas chr...

Embodiment 2

[0036] Weigh 2 grams of SiO with a Si / Al ratio of 150 2 Carrier, add 10 mL of deionized water, pipette 9 mL of H 2 PtCl 6 solution, 7.2 ml of SnCl 4 solution, 0.53 mL of KNO 3 solution and 2.0 mL of Nb(AC) 5 solution, use 2.5% ammonia water to adjust the pH value of the solution to 1, then soak in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample into a muffle furnace at 560°C ℃ for 4 hours to obtain the desired catalyst.

[0037] Catalyst evaluation conditions in the isothermal fixed-bed reactor are as follows: 0.5 g of catalyst is loaded into the above-mentioned isothermal fixed-bed reactor (the height of the catalyst bed is about 17mm), the reaction pressure is normal pressure, and the gas space velocity is 600 hours -1 , The reaction temperature is 560°C. The results are shown in Table 1.

[0038]

Embodiment 3

[0040] Weigh 2 grams of SiO with a Si / Al ratio of 150 2 Carrier, add 10 mL of deionized water, pipette 18 mL of H 2 PtCl 6 solution, 6 ml of Fe(NO 3 ) 3 solution, 30 ml of NaNO 3 solution and 1.5 mL Ta(AC) 5 Solution, adjust the pH value of the solution to 3.5 with 2.5% ammonia water, then soak in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample in a muffle furnace at 560°C ℃ for 4 hours to obtain the desired catalyst.

[0041] Catalyst evaluation conditions in the isothermal fixed-bed reactor are as follows: 0.5 g of catalyst is loaded into the above-mentioned isothermal fixed-bed reactor (the height of the catalyst bed is about 17mm), the reaction pressure is normal pressure, and the gas space velocity is 600 hours -1 , The reaction temperature is 560°C. The results are shown in Table 1.

[0042]

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Abstract

The invention relates to a mixed low carbon alkane dehydrogenation catalyst and a preparation method thereof. A problem of low activity of dehydrogenation catalysts prepared through present technologies is mainly solved. The mixed low carbon alkane dehydrogenation catalyst comprises 0.1-10% of Pt and Pd elements or oxides thereof, 0.25-10wt% of Sn, Fe, Ni elements or oxides thereof, 0.1-10wt% of Na, Li and K elements or oxides thereof, 0-10wt% of Nb, Mo, Ta and W elements or oxides thereof, and 70-99wt% of ZSM-5 with different Si/Al ratios. The mixed low carbon alkane dehydrogenation catalyst well solves the problem, and can be used in the industrial production for preparing low carbon olefins through the mixed low carbon alkane dehydrogenation.

Description

technical field [0001] The invention relates to a mixed low-carbon alkane dehydrogenation catalyst and a preparation method thereof. Background technique [0002] Propylene and isobutylene, as low-carbon olefins second only to ethylene, are widely used in chemical industry, among which propylene is mainly used in the production of polypropylene, acrylonitrile, propylene oxide, isopropanol, phenol and acetone, and isobutene is mainly used in Used in the preparation of methyl methacrylate, butyl rubber, polybutene, tert-butylamine, diisobutylene, etc. However, the current output of propylene and isobutylene cannot meet the increasing demand. It is estimated that during the 12th Five-Year Plan period, the annual growth rate of propylene demand will reach 4.8%. my country needs to import 5 million tons of propylene every year. Therefore, it is necessary to explore new sources of low-carbon olefins. With the development of oil refining industry at home and abroad, the deep proce...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/48B01J29/44C07C5/333C07C11/06C07C11/09
CPCY02P20/52
Inventor 吴省缪长喜姜冬宇刘瑞丹吴文海樊志贵
Owner CHINA PETROLEUM & CHEM CORP
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