A supported iron-nickel phosphide catalyst material and its application

An iron-nickel phosphide, supported technology, used in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, biological raw materials, etc., can solve the problem of low dispersion of active components and hydrodeoxidation capacity. Weak problems such as high activity and selectivity, large active surface, and enhanced catalytic performance

Inactive Publication Date: 2019-04-30
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] The present invention proposes a multi-component catalyst preparation method with a composite carrier plus a composite active component and a large specific surface area for the disadvantages of weak selective hydrodeoxygenation ability and low dispersion of active components in the prior art, which greatly improves Promotes the improvement of catalytic performance and has good industrial application prospects

Method used

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  • A supported iron-nickel phosphide catalyst material and its application
  • A supported iron-nickel phosphide catalyst material and its application
  • A supported iron-nickel phosphide catalyst material and its application

Examples

Experimental program
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Effect test

Embodiment 1

[0040] Prepare 0.35mol / l butyl titanate solution in absolute ethanol, take 100ml and add 35mmol dodecyldimethyl tertiary amine (DMA12) as template agent, add 35mmol glacial acetic acid while stirring, make it and Butyl titanate forms a chelate. Add 100ml of deionized water to the sol to make the colloidal particles form an open skeleton structure; at the same time, slowly add 57.53g of aluminum isopropoxide, the sol gradually loses its fluidity and forms a gel. The gel was dried at a constant temperature at 100°C for 24 hours to remove moisture, organic groups and organic solvents in the gel. Put the prepared crystal into a muffle furnace and program the temperature to 550°C for 4 hours to obtain TiO 2 -Al 2 o 3 The composite support is denoted as TiAl-1.

Embodiment 2

[0042] Prepare 0.79mol / l butyl titanate solution in absolute ethanol, take 100ml and add 78.8mmol cetyltrimethylammonium bromide (CTAB) as template agent, add 78.8mmol propionic acid while stirring, Make it form a chelate with butyl titanate. Add 100ml of deionized water to the sol to make the colloidal particles form an open skeleton structure; at the same time slowly add 43.33g of aluminum isopropoxide, the sol gradually loses its fluidity and forms a gel. The gel was dried at a constant temperature at 100°C for 24 hours to remove moisture, organic groups and organic solvents in the gel. Put the obtained crystal into a muffle furnace and program the temperature to 500°C for 4 hours to obtain TiO 2 -Al 2 o 3 The composite support is denoted as TiAl-2.

Embodiment 3

[0044] Prepare 0.60mol / l titanium tetrachloride TiCl in absolute ethanol 4 Solution, take 100ml and add 59.9mmol polyvinylpyrrolidone (PVP) as template agent, add 59.9mmol oxalic acid while stirring, make it and TiCl 4 Chelates are formed. Add 100ml deionized water to the sol to make the colloidal particles form an open skeleton structure; meanwhile slowly add 90.79g Al(NO 3 ) 3 9H 2 O, the sol gradually loses its fluidity and forms a gel. The gel was dried at a constant temperature at 100°C for 24 hours to remove moisture, organic groups and organic solvents in the gel. Put the prepared crystal into a muffle furnace and program the temperature to 550°C for 4 hours to obtain TiO 2 -Al 2 o 3 Composite support TiAl-3.

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Abstract

The object of the present invention is to provide a supported iron-nickel phosphide catalyst material, preparation method and application thereof, characterized in that: the catalyst active component is a multi-component alloy composed of Fe, Ni and P elements doped with each other compound, the catalyst support is made of TiO 2 A composite oxide support composed of a second type of component, wherein the second type of component is SiO 2 、Al 2 o 3 , ZrO 2 , CeO 2 , La 2 o 3 One or more, TiO 2 The weight percentage of the composite carrier is 5.0-95wt%, the loading amount of the catalyst active component Fe is 0.5-80wt%, the loading amount of the metal active component Ni is 0.05-30wt%, and the loading amount of the non-metallic additive P is 0.5-15wt%. The catalyst has good reactivity, stability and selectivity, and can be applied to the reaction of catalyzing the degradation of aromatic compounds from biomass oil, and can also be applied to the addition of compounds containing aromatic C-O bonds or alkyl C-O bonds. Hydrogen deoxygenation reaction.

Description

technical field [0001] The invention relates to the technical field of preparation and application of catalytic materials, in particular to a highly active iron-nickel bimetallic catalytic material and its application in the hydrodeoxygenation (HDO) reaction of substances with high aromatic ether and phenol content. Background technique [0002] As a renewable energy, bio-oil has been considered as the most potential substitute of fossil energy. However, bio-oil contains a large amount of oxygen-containing compounds such as phenols, aldehydes, alcohols and ketones, etc., and the oxygen content is as high as more than 40%. Excessive organic oxygen-containing compounds will not only increase the viscosity of the oil, but also reduce the The volatility of the oil will also reduce the stability of the oil. Hydrodeoxygenation (HDO) is currently the most important means of removing oxygen from oil in industry. Therefore, the research and development of highly active hydrodeoxyge...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J23/83C10G3/00
CPCY02P30/20
Inventor 张宗超王志光毛璟博刘凯瑞
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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