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Tandem catalyst for CO2 reduction

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Cu-based tandem catalysts can be very efficient for the selective formation of multi-carbon products via electrochemical CO2 reduction – PowerPoint PPT presentation

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Title: Tandem catalyst for CO2 reduction


1
Cu-tandem catalyst for CO2 Electroreduction
Literature Presentation Debabrata Bagchi Ph. D.
Student 17/12/2019
2
(No Transcript)
3
Novelty of the Work
  • Industrially produced CO2 is always contaminated
    with some amount of CO
  • To date catalyst development and mechanistic
    investigation based on either pure CO2 or pure CO
  • This article investigate the mechanistic pathways
    during electroreduction of CO2 in presence of CO
  • Co-feeding (CO added externally)
  • Self-feeding (CO generated locally on tandem
    catalyst)

4
Structural characterization of CuOx Catalyst
20 nm
5
CO2 to C2H4 by Electroreduction
  • Dimerization step is reported as the
    rate-determining step towards C2 products
  • Higher CO coverages enhancing the C2H4 formation
    rate.
  • Increase the bulk and local CO concentration by
    increasing the partial pressure of CO

Henry's law the amount of dissolved gas in a
liquid is proportional to its partial pressure
above the liquid.
The molar amounts of dissolved COx (CO and CO2)
in the electrolyte were calculated for each feed
using Henrys Law
J. Phys. Chem. Lett. 2015, 6, 20, 4073-4082
6
Major Product yields under mixed CO2/CO feeds
CH4
C2H4
7
Liquid product analysis at different CO2/CO feeds
8
Formate only forms in CO2-involving feeds
9
Comparison of Hydrocarbon Production Rate
  • With increasing CO in the co-feeds, the HCOO-
    pathway decreased, while the hydrocarbon yield
    sharply increased by about 50,
  • CO feeds favoured proton accessibility and C2H4
    formed via a hydrogenated dimer (COCOH)

10
Hydrocarbon yield in 11 CO2/CO co-feeds at
different potential
  • In pure CO feeds, the C2H4 yields remained low,
    suggesting a CO mass-transport limitation
    consistent with low CO solubility and local CO
    concentration at the interface

11
Post Electrochemical Characterization
  • Cu phase in both reduction process, accompanied
    by a very similar particleagglomeration for all
    feeds.
  • Observed differences in the catalytic ethylene
    yields are from kinetic mechanistic roots not
    from catalyst-related chemical factors.

12
Quantitative deconvolution of C2H4 formation
mechanism
  • Origin of two carbon of ethylene in CO2/CO feeds

CO-CO dimerization
  • Operando Differential Electrochemical Mass
    Spectrommetry (DEMS)
  • To know the atomic origin of two individual
    carbon atoms in the ethylene
  • This was achieved by using isotope-labelled 13CO
    in the feeds
  • DEMS analysis was used to verify the
    significantly enhanced C2H4 yields during cyclic
    voltammetric electrode potential scans

13
DEMS setup
  • Capillary electrochemical flow cell

Feed gas control system at DEMS setup
14
DEMS ion mass current (iMS) as function of time
11
  • The mixed feed gives enhanced C2H4 ion mass
    currents (detected via the molecular fragment
    (MH) throughout)
  • C2H4 ion mass currents on the cathodic and anodic
    sweep branches appeared to be asymmetric,
    suggesting local CO depletion due to diffusion
    limitation at the largest overpotential.

15
Deconvolution of DEMS ion mass current (iMS)
  • lower 12CO2 partial pressure to highlight the
    kinetic effects of CO in the feed.
  • Dimerization of CO2-derived surface CO in the
    cathodic sweep direction. The self-feeding supply
    of CO by CO2-to-CO is sufficient to maintain
    ethylene generation.
  • 12CO2/12CO co-feed generates comparable amounts
    of ethylene (purple curve) proving the
    suppression of local CO-depletion in anodic
    voltage sweep for pure CO2
  • Contribution of each mechanistic pathway is a
    complex function of the applied electrode
    potential and scanning direction

12 12
13
12
Im/z28
Im/z27
Im/z29
  • Evaluate the kinetic onset potentials of ethylene
    for each mechanism separately

16
Kinetic Onset Potential
  • Time-resolved, transient kinetic study to date
    where reaction mechanisms with kinetic onset
    potentials
  • Analysis revealed that the C2H4 onset potentials
    (E) shifted anodically by about 140 mV RHE when
    operating with pure CO compared to pure CO2 feeds
    (ECO2-0.81 VRHE)

17
The reaction ratio for the three mechanisms
  • A high production ratio over a large potential
    range is observed for the CO2CO mechanism,
    demonstrating a continuous contribution

18
Decomposition of the three pathways for the
co-feed
  • Comparison of the DEMS-derived cyclic mass ion
    current sweep of ethylene under CO2/CO (13)
    co-feeding, plotted in the potential domain
  • The length of the purple bars shows the enhanced
    ethylene production under CO2/CO co-feed
    conditions compared to the orange and cyan bars
    of the pure CO2 and CO feeds

19
Tafel slopes of each pathway of ethylene
formation
Lowest Tafel slope was found for the cross
coupling CO2-CO pathway, underlining the facile
reaction kinetics of the dimerization of two CO
molecules from distinct origins
20
CO2COC2H4 reaction pathways
  • Dimerization of two adsorbedCO molecules to form
    a OCCO which is further reduced to ethylene
  • Cross-coupling LH type mechanism with the
    reactive CO coming from both CO2 and CO is the
    dominant dimerization pathway
  • The existence of two distinct reactant-specific
    adsorption sites in atomic proximity on the Cu
    nanocatalyst
  • Spatially inhomogeneous distributions of
    reactant-specific 12CO and 13CO sites on the
    catalyst surface should yield products


21
From external CO2/CO co-feeds to internal
co-feeds on tandem catalysts
Another active site for CO production in
micrometre or nanometre proximity to Cu-based
CO2-reducing sites may substitute for external CO
gas
Bifunctional non-metallic/metallic tandem catalyst
NiN-functionalized carbon (NiNC) acts as
selective CO producer and is the support material
for CuOx NPs
  • SEM images of the as-prepared CuOxNiNC tandem
    catalyst illustrates the location of the two
    distinct components
  • The neighbouring CuOx NPs and NiNC are spaced on
    nanometre and micrometre scales, respectively, in
    part overlapping with each other.

22
Catalytic C2H4 performance of CuOxNiNC tandem
catalysts
  • CuOxNiNC (12) catalysts yield twice the C2H4
    production rate.
  • At overpotentials of -0.84 V RHE, CuOxNiNC
    tandem catalysts produce considerably less free
    gaseous CO compared to pure NiNC, indicating some
    of the internally generated CO is immediately
    consumed by the tandem catalysts.

23
Summary
  • Using operando DEMS, time-resolved
    isotope-labelling experiments were carried out in
    a newly designed CO2 capillary cell
  • The mechanistic pathways were quantitatively
    deconvoluted
  • Enhanced C2H4 production originated mainly from a
    cross-coupling CO2CO reaction pathway
  • Co-fed CO does not compete with CO2 for
    adsorption sites, which implies the existence of
    separate reactant specific adsorption sites for
    CO2 and CO
  • Proposing the concept of tandem catalyst for the
    utilisation of internal co-feeding.
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