Preparation method of Ni-based high-entropy oxide catalyst and its application in carbon dioxide reforming of methane to prepare syngas

Patent metadata

Field	Value
Publication number	US-12415176-B1
Application number	US-202519076057-A
Country	US
Kind code	B1
Filing date	Mar 11, 2025
Priority date	Mar 15, 2024
Publication date	Sep 16, 2025
Grant date	Sep 16, 2025

Abstract

A preparation method of a Ni-based high-entropy oxide catalyst and its application in the preparation of syngas by carbon dioxide (CO 2 ) reforming of methane (CH 4 ) is provided, and it relates to the technical field of preparation of environmental catalytic materials. The catalyst is prepared by high-energy ball milling method. Using reversible Ni particles with high content as the active site of CH 4 gas, other metals introduced by high-entropy strategy greatly reduce the carbon generated from CH 4 cracking while activate CO 2 . The prepared catalyst not only effectively overcomes the problem of poor stability of the Ni-based catalyst in CO 2 reforming of CH 4 , but also promotes activation of CO 2 and improves the efficiency of CO 2 reforming of CH 4 reaction. The provided preparation method of the high-entropy oxide catalyst is simple, stable, economical and reliable, and has a good development prospect in the industrial application field of CO 2 reforming of CH 4 technology.

First claim

What is claimed is:

1. A preparation method of a nickel (Ni)-based high-entropy oxide catalyst, comprising the following steps:
(1) mixing powders of metal sources of magnesium, zinc, cobalt and copper with a complexing agent and metal Ni to obtain a mixed product, and then ball milling the mixed product at a frequency of 20-50 hertz (Hz) for 30-60 minutes (min) to obtain a precursor;
(2) calcining the precursor obtained in the step (1) at high temperature to obtain Ni-based high-entropy oxide catalyst powder; and
(3) calcining the Ni-based high-entropy oxide catalyst powder obtained in the step (2) in a reducing gas to form reversible Ni particles, so as to obtain the Ni-based high-entropy oxide catalyst;
wherein in the step (1), a molar ratio of the metal Ni to each of the magnesium, the zinc, the cobalt and the copper is in a range of 2.6:1 to 18:1;
wherein in the step (1), the complexing agent is one or more selected from the group consisting of sodium citrate, citric acid, diethanolamine, ethylenediamine tetraacetic acid, acetylacetone, dithizone and sodium triphosphate; and
wherein in the step (2), high temperature of the calcining is in a range of 850-1200 Celsius degrees (° C.), calcination time is in a range of 1-6 hours (h), and heating rate during calcination is in a range of 1-10 Celsius degrees per minute.

2. The preparation method of the Ni-based high-entropy oxide catalyst as claimed in claim 1 , wherein in the step (1), the metal source is one or more selected from the group consisting of oxide, chloride, acetate, nitrate, carbonate, sulfate, sulfite, ammonium oxalate, citrate, and gluconate.

3. The preparation method of the Ni-based high-entropy oxide catalyst as claimed in claim 1 , wherein in the step (3), the reducing gas is hydrogen, methane (CH 4 ), or carbon monoxide; calcination temperature is in a range of 200-850° C., and calcination time is in a range of 20-200 min.

4. The Ni-based high-entropy oxide catalyst, prepared using the preparation method as claimed in claim 1 .

5. An application of the Ni-based high-entropy oxide catalyst in preparation of syngas by carbon dioxide (CO 2 ) reforming of CH 4 as claimed in claim 4 , wherein in the application, a volume ratio of the CO 2 to the CH 4 is in a range of 0.8-1.2, reaction temperature is in a range of 650-850° C., reaction pressure is in a range of atmospheric pressure to 2 megapascals (MPa), and space velocity of a reaction feed gas is in a range of 3,000-60,000 milliliters per gram per hour (mL·g −1 ·h −1 ).

Assignees

• Univ East China Science & Tech

Inventors

• Tian Chengcheng
• Wang Zhengcheng
• Zhu Xiang
• Zheng Qiying
• Yuan Cong
• Wang Hualin

Classifications

• B01J35/70

  characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title

• B01J35/30

  characterised by their physical properties · CPC title

• B01J37/18

  with gases containing free hydrogen · CPC title

• B01J37/04

  Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• C01B3/40

  characterised by the catalyst · CPC title