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Ordered mesoporous ZrO2 supported Ni catalyst and preparation method and application thereof

A catalyst and ordered mesoporous technology, which is applied to the ordered mesoporous ZrO2 supported Ni catalyst and its preparation, and the application fields of the catalytic conversion of lignin-derived phenols, which can solve the problems of poor stability, deactivation, and active components of Ni metal catalysts. It is easy to fall off and run off, and achieve the effect of large specific surface area, cost reduction, and enhanced thermal stability.

Pending Publication Date: 2020-02-04
LANZHOU 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

[0005] The invention provides an ordered mesoporous ZrO 2 Supported Ni catalyst and its preparation method and application, the catalyst is applied to the hydrodeoxygenation reaction of guaiacol, which solves the problem that the Ni metal catalyst in the prior art has poor stability and the active components are easy to fall off and lose and become inactivated question

Method used

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  • Ordered mesoporous ZrO2 supported Ni catalyst and preparation method and application thereof
  • Ordered mesoporous ZrO2 supported Ni catalyst and preparation method and application thereof
  • Ordered mesoporous ZrO2 supported Ni catalyst and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] A kind of ordered mesoporous ZrO 2 Support Ni catalyst, take the following steps to make:

[0028] (1) Dissolve 6g of zirconium n-butoxide and 2g of P123 in 30mL of absolute ethanol as solution A, wherein the specification of P123 is: average Mn~5800;

[0029] (2) Dissolve 0.45g nickel nitrate hexahydrate and 1g nitric acid in 1mL deionized water as solution B, make Ni in solution B 2+ and Zr in solution A 2+ The molar ratio is 0.1:1, and the nitric acid concentration is 65%;

[0030] (3) Slowly add solution B dropwise to solution A while vigorously stirring to obtain a sol, dry the sol in a drying oven at 40°C for 12 hours to obtain a gel, and then raise the temperature to 100°C for 12 hours to obtain a xerogel.

[0031] (4) After the dry gel is ground, it is placed in a tube furnace and heated to 400°C in air at a rate of 2°C / min and kept for 4 hours; then heated to 600°C at a flow rate of 100mL / min in hydrogen ℃, kept for 5h, the hydrogen is high-purity hydrogen ...

Embodiment 2

[0034] A kind of ordered mesoporous ZrO 2 Support Ni catalyst, take the following steps to make:

[0035] (1) Dissolve 5g of zirconium n-butoxide and 2.5g of P123 in 30mL of absolute ethanol as solution A, wherein the specification of P123 is: average Mn~5800;

[0036] (2) Dissolve 1.6g of nickel acetate tetrahydrate and 0.5g of nitric acid in 4mL of deionized water as solution B, and make Ni in solution B 2+ and Zr in solution A 2+ The molar ratio of 0.5:1, the nitric acid concentration is 65%;

[0037] (3) Slowly add solution B dropwise to solution A while vigorously stirring to obtain a sol, dry the sol in a drying oven at 40°C for 12 hours to obtain a gel, and then raise the temperature to 100°C for 12 hours to obtain a xerogel.

[0038] (4) After the dry gel is ground, it is placed in a tube furnace and heated to 400°C in air at a rate of 2°C / min and kept for 4 hours; then heated to 600°C at a flow rate of 100mL / min in hydrogen ℃, kept for 5h, the hydrogen is high-pur...

Embodiment 3

[0041] A kind of ordered mesoporous ZrO 2 Support Ni catalyst, take the following steps to make:

[0042] (1) Dissolve 8g of zirconium n-butoxide and 3g of P123 in 30mL of absolute ethanol as solution A, wherein the specification of P123 is: average Mn~5800;

[0043] (2) Dissolve 1g of nickel chloride hexahydrate and 2g of concentrated nitric acid in 6mL of deionized water as solution B, and make Ni in solution B 2+ and Zr in solution A 2+ The molar ratio of 0.2:1, the nitric acid concentration is 68%;

[0044] (3) Slowly add solution B dropwise to solution A while vigorously stirring to obtain a sol, dry the sol in a drying oven at 40°C for 12 hours to obtain a gel, and then raise the temperature to 100°C for 12 hours to obtain a xerogel.

[0045] (4) After the dry gel is ground, it is placed in a tube furnace and heated to 400°C in air at a rate of 2°C / min and kept for 4 hours; then the temperature is raised to 600°C at a rate of 100mL / min in hydrogen gas , kept for 5h, th...

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Abstract

The invention relates to an ordered mesoporous ZrO2 supported Ni catalyst and a preparation method and application thereof, and belongs to the technical fields of industrial catalysis and bioenergy conversion. A sol-gel method is adopted and polyether P123 is added to synthesize ordered mesoporous nano-ZrO2, and a nickel salt is added during the carrier synthesis process, so that the metal Ni is loaded in situ on the surface and into pores of the mesoporous ZrO2 by a one-pot method. The synthesized carrier has a large number of ordered mesoporous channels, a specific surface area, a number ofacidic sites, and a dispersion degree of Ni metal particles of the catalyst are improved, and thereby the catalytic hydrodeoxygenation activity of the catalyst for lignin-derived phenols is increased.The beneficial effects are that the used raw materials are low in cost, the preparation process is simple, a dispersion degree of the active component of the catalyst is high, the catalytic activityis high, and the catalyst has good application prospects in the field of hydrodeoxygenation refining of the lignin-derived phenols.

Description

technical field [0001] The invention relates to an ordered mesoporous ZrO 2 The invention relates to a supported Ni catalyst and its preparation method and application, specifically the application in the catalytic conversion of lignin-derived phenols, belonging to the technical field of industrial catalysis and bioenergy conversion. Background technique [0002] Lignin is a renewable biomass resource with rich sources and wide distribution, and its high-value utilization has become a research hotspot. Lignin can be decomposed by pyrolysis, liquefaction or catalysis to obtain bio-oil containing various phenolic monomers and oligomers. High value-added chemicals and liquid fuels can be further obtained by catalytic hydrodeoxygenation refining of lignin-derived phenolic compounds. The key to the research is the development of hydrodeoxygenation catalysts. [0003] Metal catalysts have been most widely used in the hydrodeoxygenation of lignin-derived phenolic compounds. Amon...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J35/02B01J35/10C07C1/20C07C13/18B01J35/00
CPCB01J23/755C07C1/20C07C2601/14C07C2523/755B01J35/40B01J35/613B01J35/615B01J35/633B01J35/647C07C13/18
Inventor 胡勋亓敬波
Owner LANZHOU INST OF CHEM PHYSICS CHINESE ACAD OF SCI