master thesis total oxidation over cu based catalysts
DESCRIPTION
The evolution in the oxidation state of Cu and Ce in a benchmark catalyst is studiedunder different conditions: temperature programmed reduction with propane and hydrogen,and isothermal reduction with propane and hydrogen.Analytical methods used involve operando X-ray absorption spectroscopy (XAS) intransmission mode at the Cu K edge and Ce LIII edge, as well as online mass spectrometry(MS) at the outlet of the reactor.TRANSCRIPT
Student : Alba Calvo GarcíaPromotor: Prof. Dr. M. F. Reyniers
Coach(es): Dr. Anilkumar Mettu, Dr. Hilde Poelman
Academic year: 2009-2010
Laboratory for Chemical Technology, Ghent University
Total oxidation over Cu based catalysts: Structure-activity relationship of metal oxides
1. Introduction: Justification, Objective, Analytical methods
2. Methodology2.1 Description of the process2.2 Experimental setup
3. Campaign November 2009 in Grenoble3.1 Synchrotron: source of X-rays3.2 Experiments
4. XANES analysis4.1 Processing of data: importing raw data, normalization4.2 Analysis of data : PCA, LCF, WL analysis
5. Results and discussion 5.1 Structure of the catalyst at ambient and pretreatment conditions 5.2 Temperature programmed reductions 5.3 Isothermal reductions
6. Conclusions
7. Future work
Overview
• Objective
Study the evolution of the active phase in CuO supported on CeO2/Al2O3 catalysts under different conditions
• Justification
Emission of VOCs: critical environmental problem → catalytic oxidation: effective technique for the elimination of VOCs
Propane: model VOC
• Analytical methods
Operando X-ray absorption spectroscopy in transmission mode at the Cu K edge and Ce L3 edge → structural information of the active phase of the catalyst during the reaction
On-line mass spectrometry → determinate the catalytic activity by measuring the concentration of the reactor effluent as a function of time
Introduction
Methodology: description of the processExperimental setup: in-situ/operando cell →
design resembles operation of a reactor under plug flow conditions
''Heart'' of the experimental cell: quartz capillary tube mounted horizontally in the setup (inner diameter 0.9mm, outer diameter 1mm) → undiluted ground catalyst (75-100µm) loaded between two glass wool plugs
Characterization of the catalyst: XAS → evaluation of unoccupied electronic states. Need for a source of X-rays
X-ray absorption coefficient (μ(E)) of a material is measured as a function of energy It = I0e − μx (Beer-Lambert‘s law)
Synchrotron radiation: used to provide a continuous source of photons → range 0.1–10 keV
Campaign November 2009, Grenoble: ESRF
All data were collected at the beamline 26 in the ESRF (European Synchrotron Radiation Facility) in Grenoble, France.
eMethodology: experimental setup
E xperimental setup in the beamline 26 (ESRF Grenoble, France)
Normal sequence of operation : Purging the setup in He, as it is an inert gas Calibrating the mass spectrometer with different gases Pre-treating the catalyst with oxygen 423K, 1h Purging the reactor with He Feeding the mixture and performing the experiment
Campaign November 2009, Grenoble: Experiments
ExperimentQuick C3H8-
TPRQuick H2-
TPR
Isothermal C3H8-
reduction
Isothermal H2-reduction
Total oxidation
Gas inlet (%) 5%C3H8/He 5%H2/He 5%C3H8/He 5%H2/He1%C3H8-
10%O2/He
T Cu K edge (ºC)
200 to 450ºC200 to 450ºC
300 to 450ºC per 50ºC
200 to 450ºC per 50ºC
300 to 400ºC per 50ºC
T Ce L3 edge (ºC)
100 to 400ºC -300 to 400ºC
per 50ºC200 to 400ºC
per 50ºC300 to 400ºC
per 50ºC
Pressure (atm)
1 1 1 1 1
Total flow (mol/s)
1.5 10-5 mol/s1.5 10-5
mol/s1.5 10-5
mol/s1.5 10-5 mol/s
0.5 - 1.5 10-5 mol/s
Experiments performed at the beam line 26:
Time resolution: fast scans → 1min/spectra; slow scans → 6, 15 or 20 min/spectra
2. Normalization → µ(E) = (µ (E) - µ0(E))/ µ0 (E0)
2.1. Value of E0 2.2. Pre-edge and post-edge 2.3. Normalized μ
(E)
XANES analysis: processing of dataAthena: interactive graphical utility for processing EXAFS data
1. Import raw data
3. Data analysis
XANES analysis: processing of dataData analysis
PCA (Sixpack): number of principal components to describe the evolution in a given set of spectra.
IND function number of components
Target transormation
Good selection of principal components
Acceptable SPOIL number (<6)
Good fitting of reference spectra
LCF analysis
XANES analysis: processing of dataData analysis
LCF (Athena): fits a linear combination of standard spectra to an unknown spectrum.
Different libraries of references:
pellets
Cu2+, Cu1+, Cu0 CuO, Cu2O, Cu capillaries
merged files
first spectrum, Cu2O reference,
last spectrum
pellets
Ce4+, Ce3+ CeO2, CeF3 capillaries
merged files
Molar fractions of Cu2+, Cu1+, Cu0 or Ce4+, Ce3+ vs T
XANES analysis: processing of dataData analysis
WL analysis: estimating the average oxidation state of Cu/Ce in each spectrum
Cu2+, Cu1+, Cu0 / Ce4+, Ce3+ references
EWL oxidation state
linear relationship : Ox. State = f(EWL)
EWL unknown spectra T unknown spectra
Oxidation state vs T
Reduction of the active phase causes a shift in the WL
Results and discussion: Initial structure of the catalystStructure of the catalyst at ambient and pretreatment conditions
Cu K XANES (references + catalyst) Ce L3 XANES (references + catalyst)
Cu2+ and Ce4+ species are present in the catalyst as prepared, the
active phase remains in its state during heating in He and after
pretreatment with oxygen
• weak pre-edge feature at 8978eV
• Shoulder feature at 8986eV
• White line at 8998eV
• Shoulder feature at 5721 eV
• White line 5731 eV
Results and discussion: Temperature programmed reductions
C3H8 TPR
Cu K XANES Ce L3 XANES
WL↓ and shifts to ↓energiesShoulder feature →Pre-edge peak ↓ 2 trends: Cu1+
and Cu0
Changes less appreciable in Ce L3 WL↑and shifts slightly to ↓energiesPronounced shoulder on the low energy side of the WL
References + catalyst after reduction
Results and discussion: Temperature programmed reductionsC3H8 TPR
Cu K XANES Ce L3 XANES
Final ox. state (400⁰C)= 3,8
Reduction 280-300 ⁰C100% Cu0 obtainedCu2O (300-450⁰C)
↓ max 380 ⁰C
Final ox. state (446⁰C) ≈ 0
↑T ↑reduction
Only 20,9% Ce3+ obtained
Results and discussion: Temperature programmed reductions
H2 TPR
Cu K XANES
Reduction with H2 → faster WL ↓ and shifts rapidly to ↓energiesShoulder feature →Pre-edge peak (Cu0)
CuO reference + catalyst at 226ºC
All spectra resemble Cu0 except for the first (226⁰)226⁰ → Catalyst is not totally oxidized
Cu K XANES
Results and discussion: Temperature programmed reductionsH2TPR
Cu K XANES
3 principal components → first one much more weight
EWL values are close to Cu0 except for the first one
Initial ox. state (226⁰C)= 1,2T ≥ 250⁰C → Ox. State ≈ 0
Results and discussion: Isothermal reductionsCu K XANES
T ≥ 250⁰C → Ox. State ≈ 0
T = 300⁰C → hardly reducedT > 350 ⁰C → Cu0
T = 350 ⁰C → features Cu2O
T ≥ 250⁰C → Spectra resemble the one of Cu0
Reduction with H2 starts at lower temperatures and occurs faster
Isothermal reduction with C3H8 Isothermal reduction with H2
Results and discussion: Isothermal reductionsCe L3 XANES
Isothermal reduction with C3H8 Isothermal reduction with H2
CeO2 is hardly reduced by C3H8, even at high T
Reduction ↑ by using H2 Bigger changes in the spectra
CeO2 and CeF3 references + catalyst at 400ºC
Pronounced shoulder on the low energy side of the WL
Results and discussion: Isothermal reductions
Isothermal reduction with C3H8 Isothermal reduction with H2
Ce L3 XANES
200ºC→Reduction starts (2 scans)
↑T isothermal reduction → ↑ final %CeF3
CeO2 is hardly reduced by C3H8
Final Ox. state (400⁰C)= 3,73
Reduction↑ by using H2 → 60,9% CeF3
Final Ox. state (400⁰C)= 3,04 (WL&LCF)
Conclusions• Study of X-ray data → evolution of the copper and cerium phase of the catalyst during the different experiments: starting temperature, activity, average oxidation state…
• At ambient conditions, heating in He and after pretreatment with oxygen, the catalyst is totally oxidized → Cu2+ and Ce4+ are the only species present
• Both Cu and Ce are active in the catalyst → differences: range of T, extent of reduction
• CuO reduction → 3 principal components; CeO2 reduction → 2 principal components • Reduction increases with T (CuO &CeO2 ) • T< 300ºC neither CuO nor CeO2 can be reduced by C3H8. Reduction with H2 starts at about 200ºC and occurs faster
• T ≥ 400ºC CuO is totally reduced by C3H8 or H2
• CeO2 is only slightly reduced by C3H8, even at high temperatures. Higher concentration of Ce3+ is obtained with H2
• A transient phase of Cu2O appears during the reduction of CuO : C3H8 (300 - 450ºC) ; H2 reduction : almost negligible (t resolution), appears at lower temperatures (200-250ºC ) → redox cycles occur via the following mechanism: CuO ↔ Cu2O ↔ Cu
Future work
- Synchronize temperature in XAS and MS measurements
- MS measurements should be performed on other gases apart from
the compounds involved in the reaction → detect leaks or capillary
breakage
- Experiments could be done in a Cu based catalyst and a Ce based
catalyst separately → how each element in the catalyst works
- XANES analysis in the Ce K edge could be performed → Better
resolution with the contribution of different coordination cells.
- XAS data could be examined in the EXAFS region as well →
structural information (distances between atoms, coordination
number..)
Thanks for your attention