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www.sciencemag.org/cgi/content/full/339/6127/1590/DC1
Supplementary Material for
Tuning Selectivity in Propylene Epoxidation by Plasmon Mediated Photo-Switching of Cu Oxidation State
Andiappan Marimuthu, Jianwen Zhang, Suljo Linic*
*Corresponding author. E-mail: [email protected]
Published 29 March 2013, Science 339, 1590 (2013)
DOI: 10.1126/science.1231631
This PDF file includes:
Materials and Methods
Figs. S1 to S6
References (30, 31)
Supplementary Material
Tuning selectivity in propylene epoxidation by plasmon mediated photo-switching of Cu oxidation state
Andiappan Marimuthu, Jianwen Zhang, Suljo Linic*
Department of Chemical Engineering, University of Michigan, Ann Arbor, MI 48109, USA.
*Correspondence to: [email protected]
This file includes:
Materials and Methods
Figs. S1-S6
References (30,31)
Materials and Methods
Section S1. Preparation of catalyst: Copper nanoparticles catalysts were prepared using (water
in oil) micro emulsion synthesis method reported previously (30). n-heptane (99% purity, Sigma-
Aldrich Cat. No. 246654), polyethylene glycol-dodecyl ether (average Mn ~362, Sigma-Aldrich
Cat. No. 235989), copper nitrate (99.999%, Sigma-Aldrich Cat. No. 229636) and hydrazine
(98% purity, Sigma-Aldrich Cat. No. 215155) were used as continuous oil phase, surfactant,
copper precursor and reducing agent, respectively. Water to surfactant (molar) ratio of 30 and
reducing agent to precursor ratio of 10 were used for the synthesis. Briefly, an aqueous solution
of copper precursor (0.1 M Cu(NO3)2) was added to the mixture of n-heptane and surfactant
(16.54 wt%) under inert atmosphere (argon). After the mixture was equilibrated, an aqueous
solution of reducing agent (1 M hydrazine) was added drop by drop to the mixture and the
microemulsion was kept under continuous stirring in inert atmosphere (argon) at room
temperature for the complete reduction of copper precursor. A known amount of support
material, SiO2, (Surface area ~80-100 m2/g, Alfa Aesar, Product No. 42737) was then added
under stirring to the microemulsion containing copper nanoparticles to prepare catalyst with final
composition of ~2 wt % Cu/SiO2. Acetone was then added to the mixture under stirring to break
the microemulsion and remove the surfactant. The catalyst was further washed with water and
ethanol by centrifugation and dried in argon at room temperature. The scanning electron
microscope (SEM) images of the copper nanoparticles synthesized showed that the particles are
quasi-spherical in shape with average size of 41 ± 9 nm. A representative SEM image of the
copper nanoparticles is shown in Figure S1. Micrographs were obtained using an FEI Nova 200
Nanolab and the accelerating voltage used for the imaging was 10 kV.
Section S2. Reactor studies: The reactions were performed in a vertically oriented packed bed
reactor (Harrick High Temperature Reaction Chamber) that allowed both temperature control
through electrical heating at the bottom and light illumination through 1cm2 silica window at the
top of the reactor (8). The light source (Dolan-Jenner Fiber-Lite 180 Model illuminator with
single gooseneck fiber optics) used for the photothermal studies (light on) was a broadband
visible light source with a maximum spectral intensity at ~580 nm (Figure S2). The source
intensity was varied by controlling the source power and the total light intensity was measured
using the combination of UV intensity meter (OAI Instruments) and CCD camera (Avantes
AvaSpec-2048). For the wavelength dependent phototothermal experiments, optical filters
(Edmund Optics) were used to control the wavelength of light reaching the catalyst from the
light source and the total intensity of light reaching the catalyst surface was kept constant (~ 550
mW/cm2) for all experiments by adjusting the power to the light source. The catalyst (packed)
bed was prepared by loading 10 mg of inert silica beads (Silica gel, Sigma-Aldrich Cat. No.
214418) to the bottom of the reactor and 12 mg of 2 wt% Cu/SiO2 catalysts on top of the layers
of silica beads. For all reactions reported here, the catalysts were pre-reduced at 523K for 1 hr in
20% hydrogen (remaining helium) at a total flow rate of 100 cm3/min before starting the
reactions. For propylene epoxidation reaction, the reactants with a composition of 50%
propylene and 50% oxygen at a total flow rate of 100 cm3/min were delivered from the top of the
catalyst bed under specified reaction conditions. The reactants and products were analyzed
online using a gas chromatograph (Varian CP 3800) equipped with thermal conductivity and
flame ionization detectors.
The rate and selectivity results reported here for thermal (light off) and photothermal (light on)
conditions were measured in a differential reactor set-up in the regime limited by the reaction
kinetics under steady state reaction conditions. Propylene oxide (PO), acrolein (Acr) and carbon
dioxide (CO2) were observed as the principal products. The reaction rates were calculated using
the formula, (CPO+CAcr+CCO2/3)/W, where, CPO, CAcr, CCO2 and W denote the measured
concentration of the products- PO, acrolein and CO2, and the weight of the catalyst, respectively.
The PO, acrolein and CO2 selectivity were calculated using the formulae-
CPO/(CPO+CAcr+CCO2/3), CAcr/(CPO+CAcr+CCO2/3) and (CCO2/3)/(CPO+CAcr+CCO2/3), respectively.
The reaction rate and selectivity data shown in the figures represent the average values of the
results obtained from multiple independent experiments and the error bars in the data represent
the standard deviations. The selectivity to all carbon-based reaction products at T = 473 K as a
function of light intensity is shown in figure S3. The selectivity of all carbon-based products as a
function of temperature at light intensity of 550 mW/cm2 is shown in figure S4. The selectivity
to all carbon-based products as a function of temperature for non-illuminated catalysts is shown
in figure S5.
Section S3. Characterization of catalyst: UV-Vis extinction spectra of the catalysts were
measured using Thermo Scientific Evolution 300 UV-Vis Spectrophotometer with a Harrick
Praying Mantis Diffuse Reflection Accessory. Harrick High Temperature Reaction Chamber
used to carry out reactions under thermal and photothermal conditions is equipped with silica
windows which allow recording of the UV-Vis spectra of the catalyst under in situ conditions.
All in situ UV-Vis measurements were acquired under inert atmosphere (100 cm3/min of helium)
at specified temperature. For in situ UV-Vis measurements under photothermal conditions (light
on), the experiments were first carried out as described in the previous section. Before measuring
the UV-Vis spectrum, the flow of reactants (100 cm3/min) was exchanged for helium (100
cm3/min) for ~15 minutes. The light source used for the photothermal experiments was then
turned off and the UV-Vis spectrum was measured in inert atmosphere (100 cm3/min of helium).
The identical procedure was followed for measuring the in situ UV-Vis spectra of the catalysts
under thermal conditions.
X-ray diffraction (XRD) patterns of the used catalysts were acquired using Rigaku Miniflex
DMAX-B rotating anode X-ray diffractometer with Cu-Kα radiation source operated at 30 kV
and 15 mA.
Section S4. Finite-difference Time-domain (FDTD) simulation: Finite-difference time-
domain (FDTD) optical simulations were performed to simulate the extinction cross section of
the copper nanoparticle as a function of wavelength of incident light. Drude-Lorentz model was
used to represent the optical properties. The empirical optical constants of copper metal were
taken from Palik (31). The periodic boundary conditions were used in x- and y-directions, while
the perfectly matched layer (PML) boundary condition was used in the z-direction. The
extinction cross sections as a function of wavelengths were calculated using the total-
field/scattered-field (TFSF) formalism. The incident light source used for the simulation was
400-1000 nm Gaussian source.
Fig. S1. Top: SEM image of copper nanoparticles dispersed on SiO2 support. Smaller particles are Cu. Bottom: SEM image of copper nanoparticles deposited on a silicon wafer.
Fig. S2. Spectrum of the light source used in the photothermal studies.
0
0.2
0.4
0.6
0.8
1
400 500 600 700 800 900 1000
Rela
tive
Inte
nsity
(a.u
)
Wavelength (nm)
Light Source
Fig. S3. Selectivity to PO, acrolein and CO2 under photothermal conditions at 473K as a function of light intensity. The selectivity data shown in the figure represent the average values of the data obtained from five independent experiments and the error bars represent the standard deviations.
0
10
20
30
40
50
60
70
100 300 500 700 900
Sele
ctiv
ity (%
)
Intensity (mW/cm2)
CO2AcroleinPO
Fig. S4. Selectivity to PO, acrolein and CO2 for photothermal (light on) process as a function of temperature. The light intensity used for the photothermal studies was 550 mW/cm2. The selectivity data shown in the figure represent the average values of the data obtained from three independent experiments and the error bars represent the standard deviations.
0
10
20
30
40
50
60
70
470 490 510 530 550
Sele
ctiv
ity (%
)
Temperature (K)
CO2
Acrolein
PO
Fig. S5. Selectivity to PO, acrolein and CO2 under thermal conditions (light off) as a function of temperature. The selectivity data shown in the figure represent the average values of the data obtained from three independent experiments and the error bars represent the standard deviations.
0
10
20
30
40
50
60
70
520 540 560 580
Sele
ctiv
ity (%
)
Temperature (K)
CO2AcroleinPO
Fig. S6. Extinction spectrum of copper spherical nanoparticle (41 nm) calculated from FDTD simulation.
0
0.2
0.4
0.6
0.8
1
1.2
1.4
400 500 600 700 800 900 1000
Extin
ctio
n cr
oss s
ectio
n x
1015
(m2 )
Wavelength (nm)
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