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Catalyst for producing olefin through dehydrogenation of pentane or hexane, preparation method and applications thereof

A catalyst and a technology for producing olefins, which are applied in the field of catalysts and preparations for pentane or hexane dehydrogenation to olefins, can solve the problems that cannot be fully utilized, that alkanes cannot be etherified, etc., and achieve good catalytic activity and stability, Effect of increasing stability, good technical effect

Active Publication Date: 2016-11-23
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] However, in addition to olefins, there are a large amount of alkanes in the C5-C6 fractions separated from FCC gasoline, and these alkanes cannot be etherified in the TAME process and cannot be fully utilized
But so far, there is almost no research on C5~C6 alkane dehydrogenation catalysts and methods

Method used

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  • Catalyst for producing olefin through dehydrogenation of pentane or hexane, preparation method and applications thereof
  • Catalyst for producing olefin through dehydrogenation of pentane or hexane, preparation method and applications thereof
  • Catalyst for producing olefin through dehydrogenation of pentane or hexane, preparation method and applications thereof

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Experimental program
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Effect test

Embodiment 1

[0042] The preparation of embodiment 1 alumina carrier I

[0043] Add 0.5 mol / L sodium hydroxide aqueous solution dropwise to 100 mL 1.0 mol / L aluminum nitrate solution until the pH of the aluminum salt solution is 8, forming a precipitate, and suction filtration and washing until the pH of the filtrate is 7 to obtain aluminum hydroxide Gel, the gel is peptized with 1.0mol / L nitric acid, the amount of acid added is H + / Al=0.25, to obtain a sol, add 15 grams of hexamethylenetetramine, then transfer the sol to a hydrothermal kettle and age it at 140°C for 10 hours, then transfer it to a beaker and dry it at 120°C, and put it in a muffle furnace Calcined at 800°C for 4 hours to obtain calcined alumina carrier I.

Embodiment 2

[0044] Embodiment 2 preparation of alumina carrier II

[0045] Add 1.0 mol / L ammonia solution dropwise to 200 mL 0.5 mol / L aluminum chloride solution until the pH of the aluminum salt solution is 8, forming a precipitate, and suction filtration and washing until the pH of the filtrate is 7 to obtain aluminum hydroxide condensate Gel, the gel is peptized with 0.5mol / L hydrochloric acid, the amount of acid added is H + / Al=0.3, to obtain a sol, add 18 grams of hexamethylenetetramine, then transfer the sol to a hydrothermal kettle and age it at 145°C for 8 hours, then transfer it to a beaker and dry it at 120°C, and put it in a muffle furnace Calcined at 650° C. for 4 hours to obtain calcined alumina carrier II.

Embodiment 3

[0046] Embodiment 3 preparation of alumina carrier III

[0047] Add 2.0 mol / L ammonia solution dropwise to 200 mL 0.5 mol / L aluminum sulfate solution until the pH of the aluminum salt solution is 8, forming a precipitate, and suction filtration and washing until the pH of the filtrate is 7 to obtain aluminum hydroxide gel , the gel is peptized with 0.5mol / L sulfuric acid, and the amount of acid added is H + / Al=0.5, to get a sol, add 32 grams of hexamethylenetetramine, then transfer the sol to a hydrothermal kettle and age it at 130°C for 18 hours, then transfer it to a beaker and dry it at 120°C, and put it in a muffle furnace Calcined at 550° C. for 4 hours to obtain calcined alumina carrier III.

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Abstract

The present invention provides a catalyst for producing olefin through dehydrogenation of pentane or hexane, wherein alumina prepared through a sol-gel method is adopted as a carrier, one or more than two selected from Rh, Ru, Pt and Pd are adopted as main active components, and one or more than two selected from Cr, Ce, In, Sn and Mo, and one or more than two selected from K, Na or Mg, and Ca are adopted as auxiliary active components. The invention further provides a specific preparation method of the catalyst, and specific application conditions for catalyzing pentane or hexane to perform dehydrogenation so as to prepare olefin, wherein the reaction temperature for olefin production is 450-600 DEG C, the reaction pressure is 0.05-0.5 MPa, the liquid volume space velocity is 1-20 h<-1>, and a hydrogen hydrocarbon molar ratio is 0.25-10:1. According to the present invention, the used catalyst adopting the alumina as the carrier has characteristics of high catalytic activity, high olefin selectivity, and good catalytic stability.

Description

technical field [0001] The invention relates to catalyst technology, in particular to a catalyst for dehydrogenating pentane or hexane to olefins and its preparation method and application. Background technique [0002] Motor gasoline has always been one of the most important products of the oil refining industry in all countries in the world. High-octane gasoline is blended from base fuel oil, high-octane blending components and a small amount of additives, among which high-octane blending components are used in a large amount, accounting for about 10% of the total gasoline. In order to increase the octane number of gasoline, alkyl lead is the longest, most economical and most commonly used gasoline additive, but its use is limited due to its strong toxicity and environmental pollution. In my country, the production of 70 # Gasoline, all produced 90 # and above gasoline. In 2003, unleaded gasoline was realized, and by 2005, the production of leaded gasoline was complete...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/63B01J23/62B01J23/652C07C11/10C07C11/107C07C11/113C07C5/333
Inventor 孙承林顾彬李先如荣欣时宇
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI