CN110404532B - 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法 - Google Patents

一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法 Download PDF

Info

Publication number
CN110404532B
CN110404532B CN201910824772.XA CN201910824772A CN110404532B CN 110404532 B CN110404532 B CN 110404532B CN 201910824772 A CN201910824772 A CN 201910824772A CN 110404532 B CN110404532 B CN 110404532B
Authority
CN
China
Prior art keywords
noble metal
solution
carrier
solvent
catalyst
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201910824772.XA
Other languages
English (en)
Other versions
CN110404532A (zh
Inventor
黄凯
雷鸣
杜鹏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhongmin Yunzhi Beijing Technology Co ltd
Original Assignee
Beijing University of Posts and Telecommunications
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing University of Posts and Telecommunications filed Critical Beijing University of Posts and Telecommunications
Priority to CN201910824772.XA priority Critical patent/CN110404532B/zh
Publication of CN110404532A publication Critical patent/CN110404532A/zh
Application granted granted Critical
Publication of CN110404532B publication Critical patent/CN110404532B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42Platinum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/468Iridium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/656Manganese, technetium or rhenium
    • B01J23/6562Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8913Cobalt and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/892Nickel and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/02Sulfur, selenium or tellurium; Compounds thereof
    • B01J27/04Sulfides
    • B01J27/047Sulfides with chromium, molybdenum, tungsten or polonium
    • B01J27/051Molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/20Carbon compounds
    • B01J27/22Carbides
    • B01J27/224Silicon carbide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/24Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/33Electric or magnetic properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0027Powdering
    • B01J37/0036Grinding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/341Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
    • B01J37/343Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation of ultrasonic wave energy

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Health & Medical Sciences (AREA)
  • Plasma & Fusion (AREA)
  • Toxicology (AREA)
  • Catalysts (AREA)

Abstract

本发明涉及一种湿化学研磨法制备贵金属纳米团簇或单原子催化剂的方法,属于材料科学与工程技术和化学领域。本发明方法制备的催化剂为以介孔金属氧化物(Co3O4、MnO2、NiCoO2以及TiO2)、氮掺杂介孔碳、导电炭黑XC72R等载体负载的团簇或原子级分散金属Pt、Ir。首先配置一定浓度的载体分散溶液A,分散均匀后加入贵金属前驱体溶液B,将溶液B加入到溶液A中均匀搅拌后用力研磨至粉末状态并干燥。部分载体的催化剂可通过退火处理得到单原子形态的贵金属。本发明具有大密度、高产量、高效率、适用性强等优点,相对于传统方法具有显著的优势。

Description

一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法
(1)发明名称:一种湿化学研磨法制备贵金属纳米团簇或单原子催化剂的方法。
(2)技术领域
本发明涉及湿化学研磨法制备贵金属纳米团簇或单原子催化剂的方法,属于材料科学与工程技术和化学领域。
(3)背景技术
目前,金属纳米结构(例如颗粒、团簇、单原子)负载的非均相纳米催化剂是材料科学与催化领域中的热点问题。与传统的纳米级催化剂相比,金属纳米结构能够作为在催化过程中的活性位点,提高催化剂的效率和活性;而且合理的金属与载体界面之间的结合也往往带来更好的催化选择性与稳定性。在纳米级金属负载型催化剂的研究中,保证金属活性位点的良好分散性、与载体界面结合的稳定性以及颗粒尺寸的调控对催化性能的影响一直是催化领域中的核心问题。现阶段制备金属负载型催化剂所采用的浸渍或煅烧等方法不仅过程繁琐、不易调控、产率低,而且有效的金属负载量往往十分有限。因此开发一种过程简单的大规模制备高金属负载量催化剂的方法是相关领域亟待解决的问题。
溶液浸渍法作为合成金属负载型催化剂的传统方法,其思路是将金属前驱体与载体材料均匀分散后将还原的金属纳米结构负载在基底上。实验结果表明,这一方法可以得到金属负载型催化剂,但存在的问题是金属纳米结构由于其自由能较高,在载体上的分散性以及稳定性还有待提升。本发明提出了一种通过湿化学研磨法制备贵金属团簇或者单原子催化剂的制备方法,选用载体的介孔结构或缺陷作为附着位点,通过液相研磨使金属团簇负载在载体上,通过调节搅拌吸附的时间以及后期的退火处理来控制颗粒尺寸的大小,实现了室温环境下高负载量、高分散度的贵金属负载型纳米催化剂的大规模合成。
(4)发明内容
1、本发明的目标
本发明提出了一种高负载量、高分散度的介孔金属氧化物、氮掺杂介孔碳、导电炭黑 XC72R等载体负载贵金属团簇或者单原子催化剂的制备方法。通过湿化学研磨将贵金属前驱体溶液还原成纳米级团簇,并使其均匀且牢固地分散在载体上,从而简单有效地制备负载型催化剂,并通过退火将纳米级团簇分散为单原子。这一方法可显著提高催化剂的性能,促进其大规模商业化应用进程。
2、本技术的发明要点
本发明要点如下:
(1)选取合适的溶剂配置质量-体积浓度为3.0-5.0mg/mL的载体分散液A,所述前驱体为可溶解或分散性良好的介孔金属氧化物氮掺杂介孔碳、导电炭黑XC72R等;所述的溶剂为乙醇;
(2)所述的贵金属前驱体溶液B为0.1mol/L的氯铂酸、氯铱酸、酞菁铂、四氨合硝酸铂的水溶液;
(3)在室温下,将上述步骤(1)制备的载体分散液A超声处理约20min,使其分散均匀,将(2)中所述的贵金属前驱体溶液B分别加入超声处理后的溶液,再充分搅拌约1h;
(4)将搅拌后成分均匀的溶液倒入玛瑙研钵中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,得到样品C;
(5)将部分种类的样品C在空气或者惰性气体中进行退火处理,得到贵金属状态为单原子的催化剂D。
本发明提出的湿化学研磨法制备贵金属团簇或单原子催化剂的方法,其优点在于具有步骤简单易操作、产率较高、化学性质稳定的特点。可以将化学还原得到的纳米级贵金属团簇稳定分散在载体中,并通过简单处理即可得到均匀分散的贵金属单原子催化剂,显著提升了载体材料的电化学性能。
(5)本发明的附图
图1是本发明方法制备的贵金属Pt/Ir团簇负载的介孔氧化钴(Co3O4)催化剂的透射电子显微镜图。
图2是本发明方法制备的贵金属Pt/Ir单原子负载的介孔氧化钴(Co3O4)催化剂的透射电子显微镜图。
图3是本发明方法制备的贵金属Pt/Ir团簇负载的介孔氧化钴(Co3O4)催化剂的氧析出(OER) 电催化活性与稳定性测试性能图。(a),(b),(c),(d)依次为1M KOH电解液中的极化曲线、稳定性曲线、Tafel动力学曲线以及计时电流曲线。
(6)本发明实施例
以下介绍本发明方法的实施例:
实施例1
贵金属Pt/Ir团簇负载的介孔Co3O4催化剂的制备。
首先,配置载体分散溶液A:20mL 5.0mg/mL介孔Co3O4溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入载体Co3O4分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir 团簇负载的介孔Co3O4催化剂。
实施例2
贵金属Pt/Ir单原子负载的介孔Co3O4催化剂的制备。
首先,配置载体分散溶液A:20mL 5.0mg/mL介孔Co3O4溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入载体Co3O4分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一。
采用快速升温设备(升温速率30℃/s)将所得的样品在450℃条件下于空气气氛中退火2h,即可得到贵金属Pt/Ir单原子负载的介孔Co3O4催化剂。
实施例3
贵金属Pt/Ir团簇负载的氮掺杂介孔碳催化剂的制备。
首先,配置载体分散溶液A:20mL 2.5mg/mL氮掺杂介孔碳溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取63uL的0.1mol/L氯铂酸溶液和63uL的0.1mol/L氯铱酸溶液加入氮掺杂介孔碳载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir团簇负载的氮掺杂介孔碳催化剂。
实施例4
贵金属Pt/Ir团簇负载的XC72R催化剂的制备。
首先,配置载体分散溶液A:20mL 2.5mg/mL导电炭黑XC72R溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取63uL的0.1mol/L氯铂酸溶液和63uL的0.1mol/L氯铱酸溶液加入载体XC72R分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir团簇负载的XC72R催化剂。
实施例5
贵金属Pt/Ir团簇负载的介孔二氧化钛催化剂的制备。
首先,配置载体分散溶液A:20mL 5mg/mL TiO2溶液,溶剂为乙醇;贵金属前驱体溶液 B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入介孔二氧化钛载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir 团簇负载的介孔二氧化钛催化剂。
实施例6
贵金属Pt/Ir团簇负载的介孔NiCo2O4催化剂的制备。
首先,配置载体分散溶液A:20mL 5mg/mL NiCo2O4溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入介孔NiCo2O4载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir团簇负载的介孔NiCo2O4催化剂。
实施例7
贵金属Pt/Ir团簇负载的少层MoS2催化剂的制备。
首先,配置载体分散溶液A:20mL 2.5mg/mL少层MoS2溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约40min,使载体在溶剂中分散均匀。取63uL的0.1mol/L氯铂酸溶液和63uL的0.1mol/L氯铱酸溶液加入少层MoS2载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir 团簇负载的少层MoS2催化剂。
实施例8
贵金属Pt团簇负载的介孔Al2O3催化剂的制备。
首先,配置载体分散溶液A:20mL 5mg/mL NiCo2O4溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取250uL的0.1mol/L氯铂酸溶液加入介孔Al2O3载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt团簇负载的介孔Al2O3催化剂。
实施例9
贵金属Pt/Ir团簇负载的介孔MnO2催化剂的制备。
首先,配置载体分散溶液A:20mL 5mg/mL介孔MnO2溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约20min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入介孔MnO2载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir团簇负载的介孔MnO2催化剂。
实施例10
贵金属Pt/Ir团簇负载的Mxene催化剂的制备。
首先,配置载体分散溶液A:20mL 5mg/mL Mxene溶液,溶剂为乙醇;贵金属前驱体溶液B:0.1mol/L的氯铂酸和氯铱酸溶液,溶剂为水;将载体分散液A超声处理约40min,使载体在溶剂中分散均匀。取125uL的0.1mol/L氯铂酸溶液和125uL的0.1mol/L氯铱酸溶液加入Mxene载体分散溶液中,并使用磁力搅拌器搅拌1h。将搅拌后成分均匀的溶液倒入玛瑙研钵,中用力研磨约2h至溶剂完全挥发且剩余固态物质颜色均一,经自然干燥后即得到Pt/Ir团簇负载的Mxene催化剂。

Claims (1)

1.一种湿化学研磨法制备贵金属团簇的方法,其特征在于该方法包括以下步骤:
(1)选取合适的溶剂配置质量-体积浓度为3.0-5.0 mg/mL的载体分散液A,所述载体为可溶解或分散性良好的介孔金属氧化物、氮掺杂介孔碳、导电炭黑XC72R;所述的溶剂为乙醇;
(2)配置物质的量浓度为0.1 mol/L的贵金属前驱体溶液B,所述贵金属前驱体为氯铂酸、氯铱酸、酞菁铂、四氨合硝酸铂,所述溶剂为水;
(3)在室温下,将上述步骤(1)制备的载体分散液A超声处理20min,使其分散均匀,将(2)中所述的贵金属前驱体溶液B分别加入超声处理后的溶液,再充分搅拌1h;
(4)将搅拌后成分均匀的溶液倒入玛瑙研钵中用力研磨2h至溶剂完全挥发且剩余固态物质颜色均一,得到的产物结构为贵金属团簇负载于载体之上,所述载体为介孔金属氧化物、氮掺杂介孔碳、导电炭黑XC72R材料。
CN201910824772.XA 2019-09-02 2019-09-02 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法 Active CN110404532B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910824772.XA CN110404532B (zh) 2019-09-02 2019-09-02 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910824772.XA CN110404532B (zh) 2019-09-02 2019-09-02 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法

Publications (2)

Publication Number Publication Date
CN110404532A CN110404532A (zh) 2019-11-05
CN110404532B true CN110404532B (zh) 2022-04-29

Family

ID=68369632

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910824772.XA Active CN110404532B (zh) 2019-09-02 2019-09-02 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法

Country Status (1)

Country Link
CN (1) CN110404532B (zh)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110694616B (zh) * 2019-10-28 2020-08-11 湖南大学 一种普适性制备负载型金属单原子/金属纳米颗粒的方法
CN111545229A (zh) * 2020-04-20 2020-08-18 北京邮电大学 一种超声辅助法制备MXene负载型贵金属催化剂的方法
CN111569867A (zh) * 2020-04-20 2020-08-25 北京邮电大学 一种球磨法制备负载型贵金属VOCs降解催化剂的方法
CN111450878B (zh) * 2020-05-08 2023-03-28 河南城建学院 一种基于TiO2介晶的单原子Ir脱硝催化剂及制备方法
CN111939953B (zh) * 2020-08-17 2023-03-21 杭州电子科技大学 一种高选择性制备糠醛的MXene基催化剂的制备方法
CN112591803A (zh) * 2020-12-28 2021-04-02 上海纳米技术及应用国家工程研究中心有限公司 用于检测的三氧化二锰原子簇修饰四氧化三钴纳米材料的制备及产品和应用
CN113713805B (zh) * 2021-08-09 2023-04-18 清华大学 一种Pt系催化剂的制备方法及其应用
CN113926421B (zh) * 2021-09-17 2022-12-20 浙江大学 一种铋负载无机多孔碘吸附材料及其宏量制备方法
CN113813944B (zh) * 2021-10-22 2024-03-15 上海科技大学 一种单原子铑催化剂及其制备方法和应用
CN114752947B (zh) * 2022-04-02 2024-03-08 上海升水新能源科技有限公司 一种高活性及稳定性的负载型析氧催化剂的制备方法
CN114871443A (zh) * 2022-05-31 2022-08-09 电子科技大学 一种用固态研磨法制备金纳米团簇的方法
CN115069239A (zh) * 2022-06-30 2022-09-20 北京化工大学 金属氧化物负载亚纳米团簇与单原子共存催化剂制备方法
CN114950411B (zh) * 2022-06-30 2023-10-20 中国科学技术大学 一种贵金属单原子催化剂及其制备方法以及在检测抗坏血酸中的应用
CN116273118A (zh) * 2023-02-28 2023-06-23 西安交通大学 一种碳基双金属纳米团簇催化剂的制备及其应用
CN116371403B (zh) * 2023-04-07 2024-10-01 西安泰金新能科技股份有限公司 一种负载型贵金属氧化物及其制备方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107694592A (zh) * 2017-09-28 2018-02-16 华南理工大学 超声辅助置换反应制备的单原子贵金属催化剂及其方法
CN108906113A (zh) * 2018-08-17 2018-11-30 北京化工大学 一种高负载量的贵金属单原子催化剂及其制备方法和应用
CN109201048A (zh) * 2018-10-19 2019-01-15 清华大学深圳研究生院 一种单原子催化剂及其制备方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109420515B (zh) * 2017-08-21 2021-06-22 中国科学院大连化学物理研究所 一种高分散负载型金属催化剂的制备方法

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107694592A (zh) * 2017-09-28 2018-02-16 华南理工大学 超声辅助置换反应制备的单原子贵金属催化剂及其方法
CN108906113A (zh) * 2018-08-17 2018-11-30 北京化工大学 一种高负载量的贵金属单原子催化剂及其制备方法和应用
CN109201048A (zh) * 2018-10-19 2019-01-15 清华大学深圳研究生院 一种单原子催化剂及其制备方法

Also Published As

Publication number Publication date
CN110404532A (zh) 2019-11-05

Similar Documents

Publication Publication Date Title
CN110404532B (zh) 一种湿化学研磨法制备贵金属团簇或单原子催化剂的方法
CN112403460B (zh) 基于金属-载体强相互作用的铂催化剂及其制备和应用
JP5168452B2 (ja) 燃料電池用電極触媒の製造方法
CN112495444B (zh) 一种TiO2@HKUST-1复合光催化剂制备方法及应用
CN111450868B (zh) 一种利用三聚氰胺甲醛树脂制备金属单原子材料的方法、金属单原子材料及其应用
CN111545229A (zh) 一种超声辅助法制备MXene负载型贵金属催化剂的方法
CN106784900B (zh) 铂基纳米颗粒包覆二氧化锡覆盖的碳纳米管及其制备方法
CN105431230A (zh) 在载体上形成贵金属纳米粒子的方法
CN110639549A (zh) 一种制备高稳定性贵金属单原子催化剂的普适性方法
JP2006228450A (ja) スポンジ状白金ナノシートをカーボンに担持せしめてなる白金−カーボン複合体とその製造方法
CN108258258A (zh) 一种用于燃料电池的富Cu八面体PtCu纳米催化剂的合成方法及应用
CN114672838A (zh) 一种碳基底氮配位金属单原子或团簇催化剂的制备方法及其产品和应用
CN110756197B (zh) Ni@Au核壳型纳米催化剂及其合成与应用
Gruzeł et al. Thin layer vs. nanoparticles: Effect of SnO2 addition to PtRhNi nanoframes for ethanol oxidation reaction
CN114602496A (zh) 纳米碳负载的铂铁双金属催化剂及其制备方法和在富氢气氛下co选择性氧化反应中的应用
CN109772405A (zh) 一种铁氮掺杂碳材料的制备方法
CN110339844A (zh) Fe纳米棒与Pt@Fe纳米棒催化剂及合成和应用
CN111569867A (zh) 一种球磨法制备负载型贵金属VOCs降解催化剂的方法
CN107221683A (zh) PtVFe/WC/C纳米氧还原催化剂的制备方法
CN111013625A (zh) 一种负载型PtMNX@Pt/C多组分核壳结构纳米催化剂及其制备方法
CN110931804A (zh) Pt-Ni-Cu三元合金担载CeO2复合材料制备及其甲酸催化性能研究
CN101966458B (zh) 高分散性、高负载量Ir及Ir-Pt合金纳米催化剂的制备方法
CN107185525B (zh) 八面体Pt纳米粒子负载γ-Al2O3型催化剂的制备方法
Takenaka et al. Preparation of composite catalysts composed of Pt nanoparticles and metal oxide nanosheets: Preferential formation of Pt/metal oxide interfaces
CN115472846A (zh) 碳载铑基有序金属间化合物及制备与作为催化剂的应用

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20231222

Address after: 430000, No. 58 Yong'an East Road, High tech Industrial Park, Xianning City, Hubei Province (within Guanggu South Science and Technology City)

Patentee after: XIANNING YOUWEI TECHNOLOGY Co.,Ltd.

Address before: 100876 Beijing city Haidian District Xitucheng Road No. 10

Patentee before: Beijing University of Posts and Telecommunications

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20240909

Address after: Room 302, 3rd Floor, Building 1, No. 398 Dongsheng Avenue, Wuzhen Town, Tongxiang City, Jiaxing City, Zhejiang Province, China 314500

Patentee after: Jiaxing Qifang New Materials Co.,Ltd.

Country or region after: China

Address before: 430000, No. 58 Yong'an East Road, High tech Industrial Park, Xianning City, Hubei Province (within Guanggu South Science and Technology City)

Patentee before: XIANNING YOUWEI TECHNOLOGY Co.,Ltd.

Country or region before: China

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20240918

Address after: Room 1008, Unit 1, 10th Floor, Building 2, No. 87 West Road, Building Materials City, Changping District, Beijing 102200

Patentee after: Zhongmin Yunzhi (Beijing) Technology Co.,Ltd.

Country or region after: China

Address before: Room 302, 3rd Floor, Building 1, No. 398 Dongsheng Avenue, Wuzhen Town, Tongxiang City, Jiaxing City, Zhejiang Province, China 314500

Patentee before: Jiaxing Qifang New Materials Co.,Ltd.

Country or region before: China