A transition metal-doped iridium-based composite catalyst and its preparation and use

Patent metadata

Field	Value
Publication number	US-2025347009-A1
Application number	US-202318860390-A
Country	US
Kind code	A1
Filing date	Apr 26, 2023
Priority date	Apr 28, 2022
Publication date	Nov 13, 2025
Grant date	—

Abstract

Disclosed are a transition metal-doped iridium-based composite catalyst and its preparation and use. The catalyst is essentially composed of amorphous oxides of iridium and a transition metal. The transition metal is selected from a metal of Group IVB, a metal of Group VB or a combination thereof. In terms of moles, the ratio of the content of iridium to the content of the transition metal in the catalyst is (0.4-0.7):(0.3-0.6). In the XRD spectrum of the catalyst, there is no diffraction peak corresponding to Iridium oxide in rutile phase. There is no diffraction peak corresponding to the crystalline phase of the oxide of the transition metal. The catalyst is in the form of a nano powder, has a uniform bulk structure, high catalytic activity and low usage amount of the precious metal iridium, and has excellent performance when applied to the anode of a proton exchange membrane water electrolyzer.

First claim

1 . A transition metal-doped iridium-based composite catalyst, which is substantially composed of amorphous oxide of iridium and a transition metal, wherein the transition metal is selected from a metal of Group IVB, a metal of Group VB or a combination thereof, wherein, in terms of moles, the content ratio of iridium to the transition metal in the catalyst is (0.4-0.7):(0.3-0.6), and in the XRD spectrum of the catalyst, there is no diffraction peak corresponding to Iridium oxide in rutile phase, nor is there a diffraction peak corresponding to the crystalline phase of the transition metal oxide.

2 . The iridium-based composite catalyst according to claim 1 , wherein in the XRD spectrum of the catalyst, there is a peak envelope only in the 2θ range of 10-70°.

3 . The iridium-based composite catalyst according to claim 1 , having a chemical composition as shown in the following formula: Ir x M 1-x O y , wherein M represents the transition metal, x is in the range of 0.4-0.7, and the value of y is such that the above chemical formula satisfies the principle of electrical neutrality.

4 . The iridium-based composite catalyst according to claim 3 , wherein:
the catalyst has a chemical composition represented by the formula Ir x Ti 1-x O y , wherein x is in the range of 0.4-0.7, and the value of y is such that the above chemical formula satisfies the principle of electrical neutrality; the catalyst has a chemical composition represented by the formula Ir x Nb 1-x O y , wherein x is in the range of 0.5-0.7, and the value of y is such that the above chemical formula satisfies the principle of electrical neutrality; or the catalyst has a chemical composition represented by the formula Ir x Ta 1-x O y , wherein x is in the range of 0.5-0.7, and the value of y is such that the above chemical formula satisfies the principle of electrical neutrality.

5 . The iridium-based composite catalyst according to claim 1 , wherein:
the transition metal is titanium (Ti), and the XRD spectrum of the catalyst has a peak envelope only in the 2θ range of 30-35°; the transition metal is niobium (Nb), and the XRD spectrum of the catalyst has a peak envelope only in the 2θ range of 25-40°; or the transition metal is tantalum (Ta), and the XRD spectrum of the catalyst has peak envelopes only in the 2θ ranges of 25-350 and 40-41°.

6 . The iridium-based composite catalyst according to claim 1 , wherein the Ir 4f characteristic peak of the XPS spectrum of the catalyst includes an Ir(IV) characteristic peak and an Ir(III) characteristic peak, and the catalyst satisfies: the peak area of the Ir(III) characteristic peak of the XPS spectrum of the catalyst is denoted as Q 1 , the peak area of the Ir(IV) characteristic peak is denoted as Q 2 , Q 1 /(Q 1 +Q 2 ) is denoted as Q 0 , and Q 0 is in the range of 0.2-0.6.

7 . The iridium-based composite catalyst according to claim 6 , wherein:
the transition metal is titanium (Ti), and Q 0 is in the range of 0.35-0.41; the transition metal is niobium (Nb), and Q 0 is in the range of 0.50-0.54; or the transition metal is tantalum (Ta), and Q 0 is in the range of 0.22-0.27.

8 . The iridium-based composite catalyst according to claim 1 , the molar ratio of Ir to the transition metal as determined by XPS analysis of said catalyst is denoted as M 1 , the molar ratio of Ir to the transition metal as determined by XRF analysis is denoted as M 2 , and the ratio of M 1 /M 2 is denoted as M 0 , wherein:
the transition metal is titanium (Ti), and M 0 is in the range of 1.20-1.55; the transition metal is niobium (Nb), and M 0 is in the range of 0.99-1.02; or the transition metal is tantalum (Ta), and M 0 is in the range of 0.98-1.04.

9 . The iridium-based composite catalyst according to claim 1 , wherein the catalyst is in the form of nanoparticle powder, the particle size of the powder particles is in the range of 1-10 nm, the BET specific surface area of the powder particles is in the range of 50-80 m 2 /g, and the proportion of micropore volume to total pore volume is 0-5%.

10 . A method for preparing the iridium-based composite catalyst according to claim 1 , comprising the following steps:
1) mixing an iridium source, a transition metal source, a complexing agent and a solvent, and reacting the resulting mixture at a pH of 6-10 to obtain reaction materials, wherein the transition metal is selected from a metal of Group IVB, a metal of Group VB and a combination thereof, and the complexing agent is selected from C3-C8 organic polyacids and soluble salts thereof, or combinations thereof; 2) evaporating and removing the solvent in the reaction materials obtained in step 1) to obtain an iridium-based composite catalyst precursor; and 3) calcining the iridium-based composite catalyst precursor in an oxygen-containing atmosphere to obtain the iridium-based composite catalyst.

11 . The method according to claim 10 , wherein:
the iridium source is selected from chloroiridic acid, alkali metal chloroiridates or a combination thereof; the transition metal source is selected from a titanium source, a niobium source, a tantalum source or a combination thereof, wherein the titanium source is selected from a soluble titanium salt, the niobium source is selected from an alcohol-soluble niobium compound, and the tantalum source is selected from an alcohol-soluble tantalum compound; and the solvent is selected from water, alcohols or a combination thereof.

12 . The method according to claim 10 , wherein:
the molar ratio of the iridium source calculated as iridium to the transition metal source calculated as transition metal is 0.5-2.5:1; and the molar ratio of the complexing agent to the total amount of the iridium source and the transition metal source is 1-4; the transition metal source is a titanium source, and the molar ratio of the iridium source calculated as iridium to the titanium source calculated as titanium is 0.5-2.5:1; the molar ratio of the complexing agent to the total amount of the iridium source and the titanium source is 1-2:1.

13 . The method according to claim 10 , wherein said step 1) further comprises:
1A) mixing the iridium source, the first complexing agent and water to obtain a first mixture; 1B) mixing the transition metal source, the second complexing agent and an organic solvent to obtain a second mixture, wherein the organic solvent is miscible with water and has a boiling point in the range of room temperature to 120° C.; 1C) adjusting the pH of the first mixture and the second mixture to 6-10 respectively; and 1D) mixing the first mixture with the second mixture after pH adjustment in step 1C), and further adjusting the pH of the obtained mixture to 6-10, and then obtaining the reaction materials through reaction; the first complexing agent and the second complexing agent may be the same or different, and are each independently selected from C3-C8 organic polyacids and soluble salts thereof, or a combination thereof.

14 . The method according to claim 13 , wherein:
the transition metal is niobium (Nb), the molar ratio of the first complexing agent to the iridium source calculated as iridium is 1-4:1, the molar ratio of the second complexing agent to the niobium source calculated as niobium was 1-4:1, and the molar ratio of the iridium source calculated as iridium to the niobium source calculated as niobium was 1-2.33:1; or the transition metal is tantalum (Ta), the molar ratio of the first complexing agent to the iridium source calculated as iridium is 1-4:1, the molar ratio of the second complexing agent to the tantalum source calculated as tantalum is 1-4:1, and the molar

Assignees

• China Petroleum & Chem Corp
• Sinopec Res Institute Of Petroleum Processing Co Ltd

Inventors

• Gu Fangwei
• Cheng Yunlv
• Zheng Lufan
• Zhang Cong
• Mi Wanliang
• Zhao Xikang
• Guo Lin
• Su Qianqian

Classifications

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title

• C25B9/23

  comprising ion-exchange membranes in or on which electrode material is embedded · CPC title

• C25B1/02

  Hydrogen or oxygen · CPC title

• C25B11/093

  at least one noble metal or noble metal oxide and at least one non-noble metal oxide · CPC title

• C25B1/04

  by electrolysis of water · CPC title