Angewandte
Chemie
nation it becomes clear that the Cu(100) has a higher
selectivity for ethylene at lower overpotential (vertical
dashed line in Figure 2) and there is in fact a range of
potentials on the Cu(100) surface at which a significant
amount of ethylene is produced and methane is not (À0.8 to
À1.0 V).
recent reports estimate that at typical current densities and
electrolyte concentrations, the local pH in a neutral bulk
solution of KHCO3 can be as high as 10–11.[9] Given these
results for an electrode roughness factor of 16, and the fact
that we estimate the CuCubes roughness factor to be about
20, it is reasonable to assume that the local pH during the
CO2RR over CuCubes is also somewhere around 10.5 which
could shift, somewhat, the selectivity toward ethylene. This
difference in local pH versus bulk pH is only thought to be
present on rough surfaces, and absent from single-crystal
surfaces, possibly contributing to the disconnect we see
between the CuCube and Cu(100) selectivities.
Table 1 summarizes the ethylene onset potentials for the
different surfaces investigated and they are arranged in order
Table 1: Onset potentials (V vs. RHE) for ethylene and methane
production from reducing CO2 in 0.1m KHCO3. The copper surfaces are
listed in order of ethylene onset.
The CuCube electrocatalyst presented here is one of the
most selective for ethylene over methane, implying that it
Surface
C2H4 onset potential
CH4 onset potential
Cu(Cube)
Cu(100)
Cu(Poly)
Cu(211)
Cu(111)
À0.60 V
À0.73 V
À0.74 V
À0.79 V
À0.96 V
À0.93 V
À0.90 V
À0.95 V
À0.94 V
À0.99 V
À
favors C C coupling to make multicarbon products instead of
completely reducing a single carbon to methane. The ability
to catalyze ethylene formation without significant methane
production indicates that these two products are most likely
formed through two distinct, competing pathways (see SI for
À
more discussion). Finding a surface that favors the C C
coupling pathway (such as the CuCube surface reported here)
is important for ultimately controlling the selectivity of the
CO2RR for multicarbon product formation.
of best to worst in terms of ethylene selectivity with CuCube
being far and away the best surface investigated. When
comparing the single crystals, Cu(100) has the most favorable
selectivity for ethylene production and the earliest onset
potential. Cu(211), which has (100) step sites, is the next best
in terms of ethylene selectivity, with Cu(111) being the worst
surface studied. The single-crystal study suggests that this
cubic surface structure is preferable for ethylene selectivity
compared to the close-packed (111) surface or the highly
stepped (211) surface.
Experimental Section
Polycrystalline copper disks with dimensions of 8 mm diameter,
2.5 mm high were machined from OHFC copper of 99.9% purity.
Copper single crystals of the same dimensions were purchased from
Princeton Scientific and are polished to an accuracy of < 0.1 degree
with a roughness < 0.01 micron (99.9999% pure). Copper working
electrodes were prepared by electropolishing in 85% phosphoric acid
at 2 V for 60 seconds (polycrystalline electrodes) or 20 seconds
(single-crystal electrodes). The electrodes were then directly sub-
merged in an aqueous electrolyte solution of 0.1m KHCO3 purged
with CO2. The resulting electrolyte pH was 6.8. Cyclic voltammo-
grams (CVs) were measured using an Ag/AgCl reference electrode
What the single-crystal studies fail to explain, however, is
the complete lack of methane formation on the CuCube
sample. Whereas the (100) surface is the most comparable to
the CuCube surface in terms of ethylene onset potential, the
(100) surface still makes a significant amount of methane. The
(211) surface, which has two-atom-wide terraces and (100)
steps, also produces significant amounts of methane and is less
selective for ethylene. Work performed by Hori et al.[8] on
single-crystal surfaces suggest there is an ideal terrace length
that gives the maximum ethylene to methane ratio with the
(100), largely devoid of steps, and the (211), having the
highest step density, the two extremes that give the smallest
ethylene to methane ratio. Hori found the Cu(711) surface to
be the most selective for ethylene, giving an ethylene to
methane ratio of 10:1. Due to the high selectivity of the
CuCubes, it is reasonable to conclude that the CuCube
surface either has a very high density of ethylene-selective
active sites compared to other CO2RR catalysts studied, or it
presents a new active site not found on other surfaces.
Another possibility that cannot be ruled out at this point is
that due to the rough nature of the CuCube surface, the local
pH during reaction is much higher than the bulk pH, and it is
this rise in local pH that improves the selectivity of the
CuCube surface. Previous work has demonstrated the impor-
tance of pH (bulk) on CO reduction over copper electrodes,
especially showing an earlier onset potential for ethylene at
higher pH.[4b,d] Similarly, local pH changes (not just bulk
changes) can affect the selectivity of copper electrodes, and
(Accumet),
a boron doped diamond counter electrode (CCL
Diamond), and a Biologic VSP 200 potentiostat scanning at a rate
of 5 mVsÀ1. The solution resistance was determined by electro-
chemical impedance spectroscopy measured after each CV at 10 kHz
and the potentiostat was set to compensate for 85% of the measured
IR drop. CuCube electrodes were prepared in situ by adding 4 mm
KCl to the standard 0.1m KHCO3 electrolyte and cycling the potential
of an electropolished polycrystalline copper disk between À1.15 V
and 0.9 V at 5 mVsÀ1 for three cycles until a stable CV was achieved.
Copper electrode surfaces were characterized by X-ray photoelectron
spectroscopy (XPS, PHI Versaprobe), X-ray diffraction (XRD,
Panalytic X’Pert 1), and scanning electron microscopy (SEM, FEI
XL30 Sirion). Capacitive scans (Figure S6) were used to estimate the
roughness factor of the CuCube electrode to around 20.
Online electrochemical mass spectrometry (OLEMS) was used to
detect the CO2RR products formed during each CV. The setup was
adapted from Koper et al.[10] and consisted of a mass spectrometer
(SRS CIS 300) measuring electrochemical reaction products that
enter the system through a porous Teflon frit (Porex 15–25 mm)
placed near the surface of the copper working electrode. Details of
the setup are shown in Figure S2. The principal improvement over the
previously reported system, was the use of custom copper disk holder.
This allowed the face of the working electrode to be placed vertically,
so that bubbles formed at high current density could escape from the
surface. Trapped bubbles can interfere with the mass transport of CO2
Angew. Chem. Int. Ed. 2015, 54, 1 – 5
ꢀ 2015 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
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