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Vanadium oxide supported catalyst for alkane dehydrogenation

A technology for alkane dehydrogenation and catalysts, which is applied in the direction of carbon compound catalysts, catalysts, physical/chemical process catalysts, etc., and can solve problems such as low catalytic activity or service life, complex processing steps, and low conversion rate

Pending Publication Date: 2021-06-04
SABIC GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these catalysts result in less than 20% conversion of n-butane to butene at 823K (548°C)
[0007] Although various supported potassium-doped vanadium oxide catalysts are known in the art for the non-oxidative dehydrogenation of alkanes to alkenes, these catalysts have complex processing steps and / or Low catalytic activity or lifetime

Method used

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  • Vanadium oxide supported catalyst for alkane dehydrogenation
  • Vanadium oxide supported catalyst for alkane dehydrogenation
  • Vanadium oxide supported catalyst for alkane dehydrogenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 3

[0058] (vanadium oxide / K of the present invention 2 Synthesis of O-supported catalysts)

[0059] Purchased from Sasol with 137m 2 Spherical (~2.5 mm diameter) transitional alumina supports per g surface area were used for catalyst preparation. The alumina support (ca. 100 g) was heat treated in an oven at 120° C. for 16 hours in the presence of air. After cooling to room temperature, the dried alumina support was used to prepare the catalyst by incipient wetness impregnation method. The catalyst was prepared by incipient wetness impregnation of the support with an aqueous solution of vanadyl oxalate. The required amount of vanadyl oxalate (3.97 g) and potassium nitrate (0.39 g) was dissolved in water and used for incipient wetness impregnation. Impregnation was performed by contacting the impregnation solution (12.6 mL) with the alumina support (27.93 g) at room temperature. The impregnated alumina support was then kept at room temperature for 12 hours and then dried at 1...

Embodiment 4

[0061] (vanadium oxide / K of the present invention 2 Synthesis of O-supported catalysts)

[0062] Purchased from Sasol with 207m 2Spherical (~1.8 mm diameter) transition alumina per gram surface area was used for catalyst preparation. The alumina support (ca. 100 g) was heat treated in an oven at 120° C. for 16 hours in the presence of air. After cooling to room temperature, the dried alumina support was used to prepare the catalyst by incipient wetness impregnation method. The catalyst was prepared by incipient wetness impregnation of the support with an aqueous solution of vanadyl oxalate. The required amount of vanadyl oxalate (7.56 g) and the required amount of potassium nitrate (0.39 g) were dissolved in water (22.3 mL) and used for incipient wetness impregnation. Impregnation was performed by contacting the impregnation solution with an alumina support (26.2 g) at room temperature. The impregnated alumina support was then kept at room temperature for 12 hours and the...

Embodiment 5

[0064] (catalyst characterization)

[0065] The surface area (BET) of the catalyst was determined using a Micromeritics Tristar Surface Area and Porosity Analyzer (Micromeritics Instruments, Inc., USA). Before measurement, samples (~200 mg) were evacuated at 300 °C for 2 h to remove physically adsorbed water and subjected to N 2 physical adsorption. The surface area results are given in Table 1 (surface areas of Comparative Example 1 and Inventive Example 3) and Table 2 (surface areas of Comparative Example 2 and Inventive Example 4). It was determined from the data that the catalyst prepared using vanadyl oxalate as the vanadium oxide precursor had a higher surface area than the catalyst prepared using ammonium metavanadate dissolved in oxalic acid as the vanadium oxide precursor.

[0066] Table 1

[0067]

[0068]

[0069] Table 2

[0070]

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Abstract

A catalyst for non-oxidative dehydrogenation of alkanes and a method for making and using the same is disclosed. The catalyst can include vanadium oxide derived from vanadyl oxalate. More particularly the catalyst is prepared by a method comprising the steps of: (a) contacting a transition alumina support with an aqueous solution comprising a vanadium carboxylate material solubilized therein; (b) heating the contacted alumina support to remove the water and produce a catalyst precursor material in solid form; and (c) heating the solid catalyst precursor material in the presence of an oxidizing source at a temperature of 500 to 800 DEG C to produce an alumina supported catalytic material comprising vanadium oxide. The catalyst can be further modified with an alkali metal oxide like potassium oxide, the precursor thereof being introduced with the impregnation solution.

Description

[0001] Cross References to Related Applications [0002] This application claims the benefit of priority to U.S. Provisional Patent Application Serial No. 62 / 727,277, filed September 5, 2018, the entire contents of which are hereby incorporated by reference in their entirety. technical field [0003] The present invention relates generally to the non-oxidative dehydrogenation of alkanes using a transitional alumina supported catalyst comprising vanadium oxide and optionally an alkali metal oxide. The catalyst is prepared using a vanadium carboxylate precursor material. Background technique [0004] Dehydrogenation of alkanes is a well-established process for the production of various useful hydrocarbon products such as isobutene for conversion to MTBE, isooctane, and alkylate for supplementing and enriching gasoline. Several catalytic methods are currently available for the catalytic dehydrogenation of light alkanes, including Method (Houdry, USA) Law (USA UOP company) ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/22B01J23/04B01J21/04B01J35/02B01J35/08B01J35/10B01J37/02B01J37/08B01J37/12C07C5/32C07C5/333C07C11/02C07C11/09B01J35/00
CPCB01J23/22B01J23/04B01J21/04B01J37/0201B01J37/086B01J37/12C07C5/3332C07C2521/04C07C2523/04C07C2523/22Y02P20/52B01J35/51B01J35/613B01J35/615C07C11/09B01J37/0219B01J37/0236
Inventor 比丘·M·德瓦西纳雷什·达查帕利尼吉特·J·梅莱普兰维诺德·S·奈尔
Owner SABIC GLOBAL TECH BV