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Method for producing alkenyl arene

A technology for alkalkenyl aromatic hydrocarbons and said alkalkenyl aromatic hydrocarbons is applied in the field of low-temperature alkyl aromatic hydrocarbon dehydrogenation catalysts and their preparation, which can solve the problems of poor stability, low activity and the like, and achieves improved alkalinity, high activity and accelerated reaction. effect of speed

Active Publication Date: 2021-01-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is the problem of low activity and poor stability of alkyl aromatic hydrocarbon dehydrogenation catalysts with low potassium content in the prior art, and a new method for producing alkyl aromatic hydrocarbons is provided

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  • Method for producing alkenyl arene
  • Method for producing alkenyl arene
  • Method for producing alkenyl arene

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Experimental program
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Embodiment 1

[0036] would be equivalent to 56.7 parts Fe 2 o 3iron oxide red, equivalent to 19.2 parts of Fe 2 o 3 Iron oxide yellow, equivalent to 4.55 parts K 2 Potassium carbonate of O, equivalent to 9.75 parts CeO 2 of cerium oxalate, equivalent to 2.58 parts of WO 3 ammonium tungstate, calcium carbonate equivalent to 2.38 parts of CaO, 3.16 parts of MgFe 2 o 4 , 1.68 parts of MnO 2 and 5.69 parts of sodium carboxymethylcellulose were stirred in a kneader for 1.5 hours, added deionized water accounting for 25% of the total weight of the catalyst raw material, stirred for 0.5 hour, took out the extruded strips, and extruded into particles with a diameter of 3 mm and a length of 6 mm. Put it in an oven, bake at 90°C for 2 hours, and bake at 160°C for 3 hours, then put it in a muffle furnace, and bake it at 750°C for 3 hours, then at 920°C for 3 hours to obtain the finished catalyst. The catalyst composition is listed in Table 1. The pore distribution and specific surface area of ...

Embodiment 2

[0045] Except for ZrO 2 Replace MnO 2 Except, catalyst preparation method and catalyst evaluation condition and analytical method are all identical with embodiment 1, specifically:

[0046] would be equivalent to 56.7 parts Fe 2 o 3 iron oxide red, equivalent to 19.2 parts of Fe 2 o 3 Iron oxide yellow, equivalent to 4.55 parts K 2 Potassium carbonate of O, equivalent to 9.75 parts CeO 2 of cerium oxalate, equivalent to 2.58 parts of WO 3 ammonium tungstate, calcium carbonate equivalent to 2.38 parts of CaO, 3.16 parts of MgFe 2 o 4 , 1.68 parts of ZrO 2 and 5.69 parts of sodium carboxymethylcellulose were stirred in a kneader for 1.5 hours, added deionized water accounting for 25% of the total weight of the catalyst raw material, stirred for 0.5 hour, took out the extruded strips, and extruded into particles with a diameter of 3 mm and a length of 6 mm. Put it in an oven, bake at 90°C for 2 hours, and bake at 160°C for 3 hours, then put it in a muffle furnace, and b...

Embodiment 3

[0051] Except for TiO 2 Replace MnO 2 Except, catalyst preparation method and catalyst evaluation condition and analytical method are all identical with embodiment 1, specifically:

[0052] would be equivalent to 56.7 parts Fe 2 o 3 iron oxide red, equivalent to 19.2 parts of Fe 2 o 3 Iron oxide yellow, equivalent to 4.55 parts K 2 Potassium carbonate of O, equivalent to 9.75 parts CeO 2 of cerium oxalate, equivalent to 2.58 parts of WO 3 ammonium tungstate, calcium carbonate equivalent to 2.38 parts of CaO, 3.16 parts of MgFe 2 o 4 , 1.68 parts of TiO 2 and 5.69 parts of sodium carboxymethylcellulose were stirred in a kneader for 1.5 hours, added deionized water accounting for 25% of the total weight of the catalyst raw material, stirred for 0.5 hour, took out the extruded strips, and extruded into particles with a diameter of 3 mm and a length of 6 mm. Put it in an oven, bake at 90°C for 2 hours, and bake at 160°C for 3 hours, then put it in a muffle furnace, and b...

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Abstract

The invention relates to a method for producing alkenyl arene, and mainly solves the problems of low activity and poor stability of a low-potassium catalyst under a low-temperature condition in the prior art. The method comprises the steps of performing dehydrogenation reaction on alkyl aromatic hydrocarbon serving as a raw material in the presence of an ultra-low potassium catalyst to obtain alkenyl arene, wherein the reaction temperature is 580-600 DEG C, the liquid space velocity is 0.5-1.5 h<-1>, the water ratio (weight) is 1.0-2.0, and the pressure is -40 kPa-normal pressure; the ultralowpotassium catalyst comprises iron, potassium, cerium, 0.5-5% of WO3, and 0.5-5% of CaO; according to the technical scheme, the problems are well solved, and the method can be used for industrial production of preparing alkenyl arene through dehydrogenation of alkyl arene.

Description

technical field [0001] The invention relates to a low-temperature alkylaromatic dehydrogenation catalyst with ultra-low potassium content and a preparation method thereof. Background technique [0002] Industrially, alkenyl aromatics are mainly produced by catalytic dehydrogenation of alkyl aromatics. One of the keys to this method is to select a dehydrogenation catalyst with high activity, high selectivity and good stability. The catalysts reported in patents are divided into two categories: one is Fe-K-Cr series, such as published U.S. patents 4152300, 4144197, and Chinese patent 87100517 alkylaromatic dehydrogenation catalysts. Although the activity and stability of this type of catalyst are better, However, it has been phased out because it contains chromium, which is not very friendly to the environment. The other is the Fe-K-Ce-Mo series, such as the published Chinese patent 201210021958.X, a high-cerium-content alkylaromatic dehydrogenation catalyst and its manufactu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/333C07C11/04B01J35/10B01J23/888B01J23/889
CPCC07C5/3332B01J23/002B01J23/8892B01J23/888B01J2523/00C07C2523/888B01J35/613B01J35/647C07C11/04B01J2523/13B01J2523/23B01J2523/3712B01J2523/69B01J2523/72B01J2523/842B01J2523/48B01J2523/47Y02P20/52
Inventor 宋磊朱敏缪长喜徐永繁张征湃
Owner CHINA PETROLEUM & CHEM CORP