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Bimetallic nanocomposite catalysts fabricated by area selective atomic layer deposition and applications Rong Chen , Kun Cao, Yun Lang, Jiaming Cai, Bin Shan Huazhong University of Science & Technology 2019-04-04 2019 Area Selective Deposition Workshop

Bimetallic nanocomposite catalysts fabricated by area ......Bimetallic nanocomposite catalysts fabricated by area selective atomic layer deposition and applications Rong Chen, Kun

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  • Bimetallic nanocomposite catalysts fabricated by

    area selective atomic layer deposition and applications

    Rong Chen, Kun Cao, Yun Lang, Jiaming Cai, Bin Shan

    Huazhong University of Science & Technology

    2019-04-04

    2019 Area Selective Deposition Workshop

  • Catalyst for Environment and Energy

    Q. Jia et al. ACS catal. 2016

    W. Wang et al. Adv. Mater.2017S. Zhang et al. JACS. 2014

    S. Cao et al. Catal. Sci. Technol.2017

    • Energy and Environment

    • Huge demand for noble metals

    O2

    H2

    Fuel cell

    PGM market report 2018 Feb Pt, Pd, Ru, Rh, Au, Ag

    HC,CH,NOx

    CO2,H2ON2

    Increasing

    2015 2016 2017

    Pt Pd Rh Pt Pd Rh Pt Pd Rh

    100.5 237.0 23.7 102.2 247.1 25.5 103.6 262.0 26.7

    15.5 14.1 2.0 16.1 13.3 2.3 16.1 16.4 2.3

    243.9 284.4 28.7 255.6 291.6 31.4 255.6 315.8 32.6

    185.8 200.8 23.3 189.2 210.3 23.5 189.9 205.2 23.9

    demand

    supply

    Automobile

    Chemical

    storage

    2

  • Catalyst is designed to be

    more active and in lower cost

    Core-shell Alloy Monometallic mixture

    Catalyst Design is Important

    Xie, et al. Nano. Lett. 2014

    • Single metal catalyst • Bimetallic catalyst

    Alayoglu et al. Nat. Mater. 2008S. Zhang et al. JACS. 2014

    3

  • ALD for Constructing Bimetallic Catalyst

    • Composition and thickness control by ALD

    J.W. Elam et al, Nano Lett. 2010

    • ALD technology: conformality, self-limiting surface

    W.M.M. Kessels et al. Chem. Mater. 2012

    Nanotechnology 2015 4

  • 5

    • Lattice strain

    bulkthin

    shell

    thick

    shell

    Latt

    ice

    stra

    in

    (%)

    Alayoglu et al. Nat Mater. 2008

    Mikkelsen et al. Chem. Mater.. 2014

    Maark et al. J. Phys. Chem.C. 2014

    • Ligand effect

    MethodsInteraction in Bimetallic Core-shell Catalyst

    0 10 20 30 40 50 6070.0

    70.2

    70.4

    70.6

    70.8

    71.0

    71.2

    Bin

    din

    g E

    ne

    rgy

    (eV

    )

    Au content in PtAu NPs (%)

    Pt4f

    Interaction between metals

    • Chemical state

    Nilekar et al. JACS. 2010

    ee

    • Chemisorption

    • The precise structure would lead to better understanding on reaction

    mechanism and boost catalytic performance.

  • Outlines

    • Bimetallic nanoparticles for catalysts

    • Catalysts for PROX reaction

    Pd@Pt Core-shell nanoparticles

    Facet selective Pt on Ru nanoparticles

    • Catalyst for DRM reaction

    Meshed Co coating on Ni nanoparticles

    • Summary

  • 7

    Pd@Pt : lattice matched, core shell interaction (ligand effect)

    Ru@Pt : mismatched crystal constant, lattice strain factor

    @Pt

    PdRu

    @Pt

    Lattice strain Ligand effect

    PROX: Preferential oxidation of CO

    • PROX reaction

    • expensive

    → Pt

    • high activity

    • Catalyst demand

    • high selectivity

    PROX

    1% 10ppm

    H2+

    CO

    H2+

    CO2

    Catalyst surface

    CO CO CO COCO CO

    → M@Pt

  • ALD recipe Pd Pt Ru

    Precursor

    Chamber

    temperature200 ºC 300 ºC 275 ºC

    Plus/purge

    time

    8

    O2

    2s 8s 2s 8s

    Pd(hfac)2 Formalin

    1.6s 8s 2s 8s

    MeCpPtMe3 O2

    • Growth rate on Si wafer

    Nucleation Liner growth

    50nm

    Pd, Pt and Ru ALD Processes

    1.6s 8s 3s 8s

    Ru(Etcp)2 O2

    O3

    0 100 200 300 400

    0

    3

    6

    9

    12

    15

    18

    Pd Ru

    Pt

    Film

    th

    ickn

    ess

    (n

    m)

    ALD cycles

    50nm

    precursors

    carrier gasMain chamber

    supports

  • SAMs Approach for Core-shell Structure

    Sci. Rep., 2015, 5, 8470

    Strategy for fabricating

    core shell NPs

    • Utilizing SAMs assisted area selective ALD could refine the nucleation of

    shell metal on core and obtain core shell NPs with regular ALD recipes.

    pinhole

    -CH3 endgroup

    9

  • Growth of Pt shell on Pd core

    • The size and composition of the core shell NPs can be controlled

    precisely by varying the ALD cycles.

    Core-shell structure Pt growth process on Pd

    QCM

    10

  • Activity and Selectivity for PROX Reaction

    PROX: CO+H2+1/2 O2 → CO2+H2 CO-tolerant: CO+H2+1/2 O2 → CO+H2O

    Preferential oxidation of CO in H2 (PROX) reaction

    ChemCatChem, 2016, 8, 326

    • The catalyst with 1 ML Pt shell shows optimal catalytic performance and

    minimal Pt loading, lowest Ea of it suggesting lower CO oxidation barrier.

    11

  • d-band Center Comparison between Ru@Pt & Pd@Pt

    • For Pd@Pt catalysts, Pt is coherent on Pd thus the

    d band center is influenced solely by ligand effect

    Pt(111) on Ru (001)

    (1.6% mismatch)

    Pt(111) on Pd (111)

    Lattice strain & Ligand effect Ligand effect

    100

    120

    140

    160

    180

    200

    220

    240

    260

    T50

    Ru

    Pd

    Pt

    Pd@Pt

    Te

    mp

    ratu

    re /

    C

    Ru@Pt

    • Lower d-band center leads to weaker adsorption

    of CO, which would reduce the CO poison effect

    • For Pt(111)/Ru (001) surface, the lower d band is

    the results of both lattice strain and ligand effect

    12

  • Design of Bi-functional Ru-Pt nanoparticles

    ⚫ The nanoparticles with bi-functional exposed facets shows weaker CO

    adsorption (Ru(001)/Pt(111)) and enhanced O2 dissociation(Ru(101)).

    13

  • Surface evolution and electron modification effect

    • As the Pt coating layer reaches to 5ML, the Pt coating layer becomes

    continuous and the surface properties are similar to pure Pt.

    • The 1ML Pt-Ru(001) shows lowest T50:As Ru(101) surface is gradually

    covered, the activity starts to decrease.

    78 76 74 72 70 68

    Inte

    nsit

    y (

    a.u

    .)

    Binding Energy(eV)

    (a) (b)Pt 4f 7/2Ru 3p 3/2

    70.9

    71.1

    71.2

    Pt4f 5/2

    Al 2p 71.3Pure Pt

    1MLPt-Ru001

    2MLPt-Ru001

    5MLPt@Ru

    10MLPt@Ru

    Pure Pt

    461.6462.7

    Pure Ru

    462.1

    Pure Pt

    74.4

    2200 2150 2100 2050 2000 1950 1900

    Wavenumber (cm-1)

    A

    dso

    rban

    ce (

    a.u

    .)468 466 464 462 460 458

    Binding Energy (eV)

    Inte

    nsit

    y (

    a.u

    .)

    (c)2090 cm-1

    Pt-CO

    2030 cm-1

    Ru-CO

    1MLPt-Ru001

    2MLPt-Ru001

    5MLPt@Ru

    10MLPt@Ru

    1MLPt-Ru001

    2MLPt-Ru001

    5MLPt@Ru

    10MLPt@Ru

    FTIR reveals the surface evolution

    14Submitted

  • Outlines

    • Bimetallic nanoparticles for catalysts

    • Catalysts for PROX reaction

    Pd@Pt Core-shell nanoparticles

    Facet selective Pt on Ru nanoparticles

    • Catalyst for DRM reaction

    Meshed Co coating on Ni nanoparticles

    • Summary

  • Meshed coating of Ni nanoparticles

    ⚫ Single Co component is less active in DRM reaction, the complete coating

    of Co on Ni (Co@Ni core shell structure) will decrease the reactivity

    ⚫ The meshed coated CoNi catalyst is designed to improve activity and

    coking inhibition, the Co component effectively enhance CO2 adsorption

    and activation, which helps to remove the carbon species on Ni sites

    CO2 Reforming of CH4

    Challenge: coking and sintering

    Heavy coking

    ChemSusChem 2015, 8, 3556; Science 2012, 335, 1205

    16

  • Design and Fabrication of meshed coating structure

    • First, atomically thin CoOx layers are deposited on Ni with ALD method

    • Post reduction of as deposited CoOx layers on Ni, where oxygen release from

    CoOx produces a meshed Co coating

    J. Catal., 2019 in press17

  • 18

    Fabrication method for meshed coating structure

    • Oxygen is released from CoOx, which

    produces a meshed Co coating

    CoOx ALD Reduction

    Ni Ni@CoOx Ni@Co

    Metallic phase

    oxidative phase

    Meshed Co coating on Ni

    • Metallic Co in Ni catalysts could

    stabilize the metallic phase of Ni

    component, which is beneficial for

    activity enhancement

    Chemical state of Co

  • Catalytic activity and stability

    • Excessive amount of Co coating (core shell structure) will cause Ni surface

    getting covered, resulting in decrease of activity

    • Ni@meshed-Co catalyst has outstanding long-term reaction stability than

    the pure Ni-based catalyst

    • Co stabilizes the Ni0 content and Co facilitates the adsorption and activation

    of CO2, which is beneficial to the activity enhancement

    Bare NiCore shell

    Meshed coating

    Activity Stability

    19

  • The Coking Reduction

    • The Ni@meshed-Co catalysts surface are mainly non-graphitic carbon species that

    can be activated and eliminated

    • The higher CO2 conv. produces much less CO, and meshed coating catalysts produces

    less CH* intermediates and are fast removed

    TG Raman

    20

  • Summary

    Core shell

    structure

    Facet selective

    coated structure

    Meshed like

    coated structure

    • SAMs assisted selective ALD is applied to fabricate Pd@Pt

    core shell nanoparticles, Pt coating layer can be controlled

    with atomic monolayer precision showing high activity for

    PROX reaction

    • Facet selective ALD is achieved through lattice mismatch to

    fabricate bi-functional Pt@Ru(001) structure, enhancing the

    CO activation and O2 dissociation at the same time for

    PROX reaction

    • ALD with post reduction treatment is developed to

    synthesize meshed Co coating Ni nanoparticles, which is

    highly active and coking resistant for DRM reaction