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Use of hollow zeolite doped with bimetallic or trimetallic particles for hydrocarbon reforming reactions

A bimetallic and trimetallic technology, applied in the field of catalysts, can solve the problems of adverse impacts on commercial application costs, expensive catalysts and rare metals, etc.

Inactive Publication Date: 2018-06-08
SABIC GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] Despite all the research on encapsulated metal hollow zeolite catalysts currently available, many of the catalysts obtained contain expensive rare metals, which can adversely affect the cost of commercial application

Method used

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  • Use of hollow zeolite doped with bimetallic or trimetallic particles for hydrocarbon reforming reactions
  • Use of hollow zeolite doped with bimetallic or trimetallic particles for hydrocarbon reforming reactions
  • Use of hollow zeolite doped with bimetallic or trimetallic particles for hydrocarbon reforming reactions

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0068] (Synthesis of silicalite-1)

[0069] Silica-1 is prepared by mixing ethyl orthosilicate (TEOS, purity 98%, USA) and tetrapropylammonium hydroxide (TPA(OH), 1.0M in water, United States) and water. The gel composition is: SiO 2 : 0.4TPA(OH): 35H 2 O. Then, the mixture was transferred into a Teflon-lined autoclave and heated at 170 °C under static conditions for 3 days. The solid was recovered by centrifugation and washed with water, which was repeated 3 times. The resulting solid was dried overnight at 110°C and then calcined in air at 525°C for 12 hours.

Embodiment 2

[0071] (Synthesis of Ni / hollow-silicalite-1(HZ) comparative catalyst material)

[0072] With Ni(NO 3 ) 2 ·6H 2 O aqueous solution (USA ) impregnated the silicalite-1 of Example 1 to produce 1.8 wt% Ni or 5.5 wt% Ni on silicalite-1. The suspension was dried overnight in air at 50°C. Impregnated silicalite-1 (1 g) was suspended with aqueous TPA(OH) (4.15 in 3.33 mL of water). The mixture was transferred to a Teflon-lined autoclave and heated at 170° C. under static conditions for 24 hours. Finally, 1.8NiHZ was calcined in air at 450°C for 6 hours. Table 1 lists the composition of the samples.

Embodiment 3

[0074] (General Synthesis Method of Metal Hollow-Silicalite-1 Catalyst Material)

[0075] With Ni(NO 3 ) 2 ·6H 2 O (United States ) and Co(NO 3 ) 2 ·6H 2 O(Aldrich) or RuCl 3 ×H 2 An aqueous solution of O (Aldrich) impregnated the silicalite-1 of Example 1 to prepare 5.5% by weight NiM in a 50 / 50 molar ratio on silicalite-1. 2 (NiCo or NiRu). The suspension was dried overnight in air at 50°C. Impregnated silicalite-1 (1 g) was suspended with aqueous TPA(OH) (4.15 in 3.33 mL of water). The mixture was transferred to a Teflon-lined autoclave and heated at 170° C. under static conditions for 24 hours. Finally, NiCo / HZ was calcined at 450 °C in air for 6 hours. Table 1 lists the composition of the samples.

[0076] Table 1

[0077] Sample serial number

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Abstract

Catalysts useful for hydrocarbon reforming reactions are described. A catalyst can include a bimetallic (M1M2) or trimetallic (M1M2M3) nanostructure, or oxides thereof, and a hollow zeolite support. The hollow space in the zeolite support includes the bi-metallic (M1M2) or tri-metallic (M1M2M3) nanostructure, or oxides thereof.

Description

[0001] Cross References to Related Applications [0002] This application claims the benefit of priority to U.S. Provisional Patent Application No. 62 / 248665, filed October 30, 2015, the entire contents of which are incorporated herein by reference. Background technique [0003] A. Field of Invention [0004] The present invention generally relates to catalysts for use in chemical applications (eg, hydrocarbon reforming reactions, such as dry reforming or steam reforming of methane). In particular, the present invention relates to a catalyst comprising a bimetallic (M 1 m 2 ) or trimetallic (M 1 m 2 m 3 ) nanostructures, or oxides thereof, and hollow zeolite carriers. The hollow space of the zeolite support contains bimetallic (M 1 m 2 ) or trimetallic (M 1 m 2 m 3 ) nanostructures, or oxides thereof. [0005] B. Description of related technologies [0006] Synthesis gas or "syngas" is a gas mixture comprising carbon monoxide and hydrogen. Syngas is often used a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/072B01J29/035C01B3/40B01J37/10B01J29/46B01J35/10B01J37/02
CPCB01J37/10B01J29/072B01J29/46B01J35/002B01J35/006B01J35/0086B01J35/1019B01J35/1038B01J37/0018B01J37/0203C01B3/40B01J2229/186B01J2229/22B01J2229/38B01J2229/40B01J29/0356C01B2203/0233C01B2203/0238C01B2203/1047C01B2203/1082C01B2203/1241Y02P20/52B01J23/755B01J23/892B01J29/035B01J35/0006B01J35/0013B01J37/0201B01J37/08C01B2203/1058C01B2203/1064
Inventor 乌戈·拉翁劳伦斯·德索萨维努·维斯瓦纳特
Owner SABIC GLOBAL TECH BV