Raymond J. Gorte

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Name: Gorte, Raymond
Organization: University of Pennsylvania , USA
Department: Department of Chemical & Biomolecular Engineering
Title: (PhD)

TOPICS

Co-reporter:Yu-Hao Yeh, Chen-En Tsai, Cong Wang, and Raymond J. Gorte
Industrial & Engineering Chemistry Research May 31, 2017 Volume 56(Issue 21) pp:6198-6198
Publication Date(Web):May 12, 2017
DOI:10.1021/acs.iecr.7b01006
The heat flows associated with conversion of n-hexane on H-ZSM-5 and H(Zn)-ZSM-5 were measured for reaction at 60 bar and both 673 and 773 K for application to endothermic reforming for hypersonic flight. The heat flows were determined by measuring the power required to maintain a constant reactor temperature upon introduction of flowing n-hexane. The acid-catalyzed reactions over H-ZSM-5 were found to be only mildly endothermic (<10 kJ/mol) at low conversions and exothermic at all conversions above 50%. The reactions on H(Zn)-ZSM-5 were significantly more endothermic (40–50 kJ/mol) for conversions of <70%; however, the reactions also became exothermic at very high conversions. Measurements of the product distributions showed that the reaction endothermicity for H(Zn)-ZSM-5 at lower conversions was likely due to the formation of significant amounts of benzene, toluene, and xylene, but that these were converted to higher-molecular-weight products at high conversions. Implications of these results for preparing improved endothermic-reforming catalysts is discussed.
Co-reporter:Tianyu Cao, Yuan Cheng, Raymond J. Gorte, Yixiang Shi, ... Ningsheng Cai
Ceramics International 2017 Volume 43, Issue 18(Volume 43, Issue 18) pp:
Publication Date(Web):15 December 2017
DOI:10.1016/j.ceramint.2017.09.045
Direct carbon fuel cells (DCFC) that employ solid oxide electrolytes and molten Sb anodes are promising for the efficient generation of electricity using a range of carbonaceous fuels. The present study examined the etching of yttria-stabilized zirconia (YSZ) and gadolinia-doped ceria (GDC) electrolytes by Sb2O3 produced during fuel-cell operation. Migration of Sb along grain boundaries and electrolyte corrosion were observed for both polycrystalline YSZ and GDC electrolytes; however, corrosion and electrolyte thinning were not observed for a single-crystal YSZ electrolyte, even after long-term operation. These results indicate that Sb migration along grain boundaries plays a significant role in electrolyte corrosion in DCFCs with molten Sb anodes. Several strategies for avoiding this problem are also discussed.
Co-reporter:Jing Luo, Hongseok Yun, Alexander V. Mironenko, Konstantinos Goulas, Jennifer D. Lee, Matteo Monai, Cong Wang, Vassili Vorotnikov, Christopher B. Murray, Dionisios G. Vlachos, Paolo Fornasiero, and Raymond J. Gorte
ACS Catalysis 2016 Volume 6(Issue 7) pp:4095
Publication Date(Web):May 20, 2016
DOI:10.1021/acscatal.6b00750
Carbon-supported, Pt and PtCo nanocrystals (NCs) with controlled size and composition were synthesized and examined for hydrodeoxygenation (HDO) of 5-hydroxymethylfurfural (HMF). Experiments in a continuous flow reactor with 1-propanol solvent, at 120 to 160 °C and 33 bar H2, demonstrated that reaction is sequential on both Pt and PtCo alloys, with 2,5-dimethylfuran (DMF) formed as an intermediate product. However, the reaction of DMF is greatly suppressed on the alloys, such that a Pt3Co2 catalyst achieved DMF yields as high as 98%. XRD and XAS data indicate that the Pt3Co2 catalyst consists of a Pt-rich core and a Co oxide surface monolayer whose structure differs substantially from that of bulk Co oxide. Density functional theory (DFT) calculations reveal that the oxide monolayer interacts weakly with the furan ring to prevent side reactions, including overhydrogenation and ring opening, while providing sites for effective HDO to the desired product, DMF. We demonstrate that control over metal nanoparticle size and composition, along with operating conditions, is crucial to achieving good performance and stability. Implications of this mechanism for other reactions and catalysts are discussed.Keywords: 2,5-dimethyl furan; 5-hydroxymethylfurfural; bimetallic catalyst; hydrodeoxygenation; PtCo nanocrystal
Co-reporter:Jingye Yu, Shiyu Zhu, Paul J. Dauenhauer, Hong Je Cho, Wei Fan and R. J. Gorte  
Catalysis Science & Technology 2016 vol. 6(Issue 14) pp:5729-5736
Publication Date(Web):13 Apr 2016
DOI:10.1039/C6CY00501B
The adsorption and reaction properties of H-BEA, SnBEA, ZrBEA and siliceous BEA were examined to understand the reaction of 2,5-dimethylfuran (DMF) with ethylene to form p-xylene. Temperature-programmed desorption (TPD) of diethyl ether, DMF, 2,5-hexanedione and p-xylene on each of the zeolites demonstrated that the Brønsted sites in H-BEA are more reactive than the Lewis sites in SnBEA and ZrBEA and tend to promote the oligomerization of DMF and 2,5-hexanedione, even at 295 K; however, the adsorbed 2,5-hexanedione is converted to DMF at both Lewis- and Brønsted-acid sites. H-BEA, SnBEA and ZrBEA all catalyzed the reaction to p-xylene with high selectivity in a continuous-flow reactor, with all three catalysts showing rates that were first order in both DMF and ethylene. H-BEA was found to deactivate rapidly due to coking, while ZrBEA and SnBEA were both stable. The implications of these results for practical applications are discussed.
Co-reporter:Yu-Hao Yeh, Shiyu Zhu, Patrick Staiber, Raul F. Lobo, and Raymond J. Gorte
Industrial & Engineering Chemistry Research 2016 Volume 55(Issue 14) pp:3930
Publication Date(Web):March 25, 2016
DOI:10.1021/acs.iecr.6b00639
The addition of Zn to H-ZSM-5 zeolites was studied for application to endothermic reforming in hypersonic aircraft engines. Temperature-programmed-desorption (TPD)/thermogravimetric-analysis (TGA) measurements with 2-propanamine on two H(Zn)-ZSM-5 samples showed that at low ion-exchange levels, less than 0.5 Zn/Al, each Zn cation displaces one Brønsted-acid site. Although rates for n-hexane conversion at 633 and 823 K and at a pressure of 137 bar decreased with the loss of Brønsted sites, Zn promotion greatly increased the production of H2 and the formation of small aromatic molecules. FTIR of adsorbed acetonitrile-d3 and calorimetric measurements of adsorbed CO at 195 K indicate that the exchanged Zn cations form Lewis-acid centers. A model in which the Zn cations, acting as Lewis-acid centers, polarize intermediates formed at Brønsted sites is presented as a way of understanding the observations.
Co-reporter:Jingye Yu, Jing Luo, Yiwei Zhang, Junjie Cao, Chun-Chih Chang, R.J. Gorte, Wei Fan
Microporous and Mesoporous Materials 2016 Volume 225() pp:472-481
Publication Date(Web):1 May 2016
DOI:10.1016/j.micromeso.2016.01.039
•Alkali-exchanged BEA zeolites are shown to interact strongly with Lewis bases.•Pyridine, acetonitrile, 2-methyl-2-propanol and CO interact most strongly with Li-BEA > Na-BEA > K-BEA.•Alkali-exchanged BEA are not active for alcohol dehydration or reductive etherification of HMF.The possibility of using alkali-exchanged BEA zeolites as Lewis-acid catalysts was examined using temperature-programmed desorption (TPD)/thermogravimetric analysis (TGA) measurements of adsorbed pyridine, 2-propanamine, diethyl ether, 2-methyl-2-propanol, and acetonitrile, FTIR of pyridine and CD3CN, calorimetry of CO, and reaction rates for reductive etherification of 5-hydroxymethyl furfural (HMF) with 2-propanol. Adsorption on the alkali cations occurs through ion–dipole interactions, as evidenced by the fact that adsorption is strongest on Li, followed by Na and K. Adsorption of all the probe molecules was much stronger on Li-BEA than on acid sites formed by framework Sn in SnBEA; however, the alkali-exchanged BEA samples were not catalytically active for alcohol dehydration or reductive etherification of HMF. The implications of these results for the characterization of solid Lewis acidity are discussed.
Co-reporter:Yu-Hao YehRaymond J. Gorte
Industrial & Engineering Chemistry Research 2016 Volume 55(Issue 50) pp:
Publication Date(Web):December 1, 2016
DOI:10.1021/acs.iecr.6b03659
The catalytic properties of H-[Fe]ZSM-5 and H-[B]ZSM-5 were explored after addition of Zn or Ga. TPD–TGA of 2-propanamine adsorbed on Zn- and Ga-exchanged H-[Fe]ZSM-5 showed a decrease in Brønsted-acid site densities and the formation of new dehydrogenation sites, similar to what is observed following exchange in H-[Al]ZSM-5 and in amorphous silica–alumina. Exchanged Zn cations in [Fe]ZSM-5 also exhibited Lewis-acid character, as demonstrated by the appearance of a υ(CN) stretch at 2310 cm–1 upon adsorption of CD3CN. By contrast, the sites in H-[B]ZSM-5 were not capable of protonating 2-propanamine, did not form dehydrogenation sites when Zn or Ga were added, and showed no evidence for sites with Lewis-acid character from the FTIR spectroscopy of CD3CN. Neither H(Zn)-[Fe]ZSM-5 nor H(Zn)-[B]ZSM-5 catalyzed reactions of n-hexane at 773 K, but the TPD–TGA of adsorbed propene on H(Zn)-[Fe]ZSM-5 showed strong interactions between the Zn and olefins that might be responsible for the dehydrocyclization of light alkanes in Zn-exchanged, Al-containing zeolites.
Co-reporter:Jing Luo;Matteo Monai;Hongseok Yun;Lisandra Arroyo-Ramírez
Catalysis Letters 2016 Volume 146( Issue 4) pp:711-717
Publication Date(Web):2016 April
DOI:10.1007/s10562-016-1705-x
Hydrodeoxygenation of furfural was studied over a 10-wt% Pt/C catalyst at 453 K, under both low- and high-pressure conditions. With vapor-phase furfural as the feed and H2 pressures below 1 bar, decarbonylation to furan is a major product, with the selectivity to furfuryl alcohol and dimethylfuran increasing with increasing H2 pressure. When the reaction is performed at 33 bar, using 1-wt % furfural in 1-propanol solvent and high-pressure H2, no evidence for decarbonylation was observed. At high pressures, the reaction is sequential, with all the furfural proceeding to methylfuran, which in turn reacts to over-hydrogenated products, including 2-methyltetrahydrofuran and 2-pentanone. It is suggested that the hydrogen surface coverage is responsible for the apparent differences in the reaction network at high and low pressures.
Co-reporter:Yu-Hao Yeh
The Journal of Physical Chemistry C 2016 Volume 120(Issue 22) pp:12132-12138
Publication Date(Web):May 23, 2016
DOI:10.1021/acs.jpcc.6b03855
The adsorption of a series of small alkanes was studied experimentally on H-ZSM-5 zeolites using calorimetric measurements in order to determine their interactions with the Brønsted sites. Differential heats measured on four ZSM-5 samples with different Si/Al2 ratio and with different defect concentrations were found to depend strongly on the Brønsted-site density but not on the presence of defects. The interactions for CH4 with the Brønsted sites were minimal but the effect was significant (up to 11 ± 2 kJ/mol extra heats) for larger alkanes, such as n-C6H14. The affinity of the alkanes with the Brønsted sites increased with the gas-phase proton affinity of the alkanes and the calculated affinity of the alkanes for the strong acid, fluorosulfonic acid. The extra heats of adsorption in H-ZSM-5 over its siliceous counterparts can therefore be associated with the strength of hydrogen bonding between the adsorbed alkane and the Brønsted sites, which in turn increases with molecular size. Specifically, extra heats were found to vary linearly with acid affinity corrected for dispersion interactions. The comparison of the experimental and computational results, therefore, indicates that the hydrogen bonded interaction theory describes the effect of Brønsted sites for alkane adsorption on zeolites.
Co-reporter:Tzia Ming Onn, Shuyi Zhang, Lisandra Arroyo-Ramirez, Yu-Chieh Chung, George W. Graham, Xiaoqing Pan, and Raymond J. Gorte
ACS Catalysis 2015 Volume 5(Issue 10) pp:5696
Publication Date(Web):August 24, 2015
DOI:10.1021/acscatal.5b01348
The effect of modifying Pd/Al2O3 catalysts by atomic layer deposition of 1 nm ZrO2 films was studied. For deposition on oxidized, PdO/Al2O3 catalysts, TEM imaging, EDS mapping, and metal-dispersion measurements confirmed the presence of the thin ZrO2 over both the Al2O3 support and the metal particles. The ZrO2 films were surprisingly stable, forming a well-crystallized phase only above 1173 K. The ZrO2 coating over the PdO particles created a semicore–shell-like structure that stabilized the metal against sintering in air at 1073 K. Steady-state, methane oxidation rates on unmodified PdO/Al2O3 decreased with increasing catalyst calcination temperature, but rates on the ZrO2-covered surfaces increased with increasing calcination temperature.Keywords: atomic layer deposition; improved rates; methane oxidation; palladium; thermal stability; zirconia
Co-reporter:Dr. Matteo Monai;Dr. Tiziano Montini;Dr. Chen Chen;Dr. Emiliano Fonda; Raymond J. Gorte;Dr. Paolo Fornasiero
ChemCatChem 2015 Volume 7( Issue 14) pp:2038-2046
Publication Date(Web):
DOI:10.1002/cctc.201402717

Abstract

The influence of water vapor on methane catalytic combustion was studied over a Pd@CeO2/Si-Al2O3 catalyst, carefully designed to maximize Pd-CeO2 interaction and prevent metal sintering and compared to a conventional impregnated catalyst with identical chemical composition. Although the nanostructured Pd@CeO2/Si-Al2O3 catalyst is thermally stable, the addition of water to the reaction feed leads to a transient deactivation at low temperatures, consistent with the well documented competitive adsorption. In addition to this, the hierarchically structured catalyst exhibits an additional severe deactivation after methane oxidation in the presence of water vapor at 600 °C that can be reversed only by heating the catalyst above 700 °C. The presence of water in the reaction feed deactivates the conventional impregnated catalyst less severely and the activity largely returns upon water removal. Catalytic FTIR and CO-chemisorption data indicate that this severe deactivation process in the hierarchical catalyst is due to the formation of stable OH groups on the surface of the ceria nanoparticles. These hydroxyl groups are suggested to significantly inhibit the oxygen spillover from the CeO2 nanoparticles to Pd, preventing its efficient re-oxidation, as observed by operando X-ray absorption near edge spectroscopy (XANES) experiments. At the same time, their presence can contribute to limit the gas phase accessibility of Pd, as indicated by the decrease of CO chemisorption capability. The presence of hydroxyls plays a minor role on the deactivation of the conventional catalyst at 600 °C.

Co-reporter:Dr. Matteo Monai;Dr. Tiziano Montini;Dr. Chen Chen;Dr. Emiliano Fonda; Raymond J. Gorte;Dr. Paolo Fornasiero
ChemCatChem 2015 Volume 7( Issue 14) pp:
Publication Date(Web):
DOI:10.1002/cctc.201500644

Abstract

The front cover artwork for Issue 14/2015 is provided by the groups of Prof. Raymond J. Gorte and Prof. Dr. Paolo Fornasiero. The image shows the deactivation of hierarchical Pd@CeO2 catalysts for methane combustion in the presence of water. See the Full Paper itself at http://dx.doi.org/10.1002/cctc.201402717.

Co-reporter:Dr. Matteo Monai;Dr. Tiziano Montini;Dr. Chen Chen;Dr. Emiliano Fonda; Raymond J. Gorte;Dr. Paolo Fornasiero
ChemCatChem 2015 Volume 7( Issue 14) pp:
Publication Date(Web):
DOI:10.1002/cctc.201500740
Co-reporter:A. S. Yu, J. M. Vohs and R. J. Gorte  
Energy & Environmental Science 2014 vol. 7(Issue 3) pp:944-953
Publication Date(Web):27 Jan 2014
DOI:10.1039/C3EE43137A
Ceramic membrane reactors based on Mixed Ionic and Electronic Conductors (MIEC) show great promise for the production of syngas from natural gas. Here, the principles behind this technology are briefly reviewed. By comparing these reactors to solid oxide fuel cells, for which the operating principles are nearly identical, we argue that surface reactions on the membrane frequently limit the performance of these devices. Concepts for increasing surface reaction rates and incorporating catalysts onto the surface are discussed.
Co-reporter:Jing Luo, Jingye Yu, Raymond J. Gorte, Eyas Mahmoud, Dionisios G. Vlachos and Michael A. Smith  
Catalysis Science & Technology 2014 vol. 4(Issue 9) pp:3074-3081
Publication Date(Web):02 Jun 2014
DOI:10.1039/C4CY00563E
The liquid-phase (69 bar) reaction of 5-hydroxymethylfurfural (HMF) with 2-propanol for production of furanyl ethers was studied at 413 and 453 K over a series of oxide catalysts, including γ-Al2O3, ZrO2, TiO2, Al2O3/SBA-15, ZrO2/SBA-15, TiO2/SBA-15, H-BEA, and Sn-BEA. The acidity of each of the catalysts was first characterized for Brønsted sites using TPD-TGA of 2-propanamine and for Lewis sites using TPD-TGA of 1-propanol. Catalysts with strong Brønsted acidity (H-BEA and Al2O3/SBA-15) formed 5-[(1-methylethoxy)methyl]furfural with high selectivities, while materials with Lewis acidity (γ-Al2O3, ZrO2, TiO2, and Sn-BEA) or weak Brønsted acidity (ZrO2/SBA-15 and TiO2/SBA-15) were active for transfer hydrogenation from the alcohol to HMF to produce 2,5-bis(hydroxymethyl)furan, with subsequent reactions to the mono- or di-ethers. Each of the catalysts was stable under the flow-reactor conditions but the selectivities varied with the particular oxide being investigated.
Co-reporter:Sounak Roy, Kevin Bakhmutsky, Eyas Mahmoud, Raul F. Lobo, and Raymond J. Gorte
ACS Catalysis 2013 Volume 3(Issue 4) pp:573
Publication Date(Web):February 20, 2013
DOI:10.1021/cs300599z
The adsorption properties of framework Sn sites in a siliceous zeolite beta were examined by comparing the adsorption of acetonitrile, diethyl ether, and 2-methyl-2-propanol on a Sn-Beta zeolite, a purely siliceous Beta zeolite, and a siliceous Beta zeolite with impregnated SnO2, using temperature-programmed desorption (TPD) and thermogravimetric analysis (TGA). Adsorption stoichiometries close to one molecule per framework Sn site were observed for each of the probe molecules. Although the 1:1 complexes with acetonitrile and diethyl ether decompose reversibly upon mild heating in vacuo, the 1:1 complex formed by 2-methyl-2-propanol underwent dehydration to butene and water over a very narrow temperature range centered at 410 K. FTIR spectra of acetonitrile-d3 at a coverage of one molecule per site exhibit a υ(C–N) stretching frequency at 2312 cm–1 that is not observed with nonframework Sn, providing a convenient method for characterizing the presence of framework Sn sites. Water interacts strongly enough with the Sn sites to prevent adsorption of acetonitrile.Keywords: Lewis acid base complexes; Lewis catalysis; Sn-Beta; temperature programmed desorption; tin zeolites
Co-reporter:Jing Luo;R. J. Gorte
Catalysis Letters 2013 Volume 143( Issue 4) pp:313-316
Publication Date(Web):2013 April
DOI:10.1007/s10562-013-0964-z
The cracking of n-hexane over H-ZSM-5 has been studied at pressures from 0.03 to 137 bar, between 558 and 633 K, for application to endothermic reforming. The rates showed the effects of saturated adsorption for n-hexane in the zeolite, with the reaction being first-order at low pressures and zeroth-order at high pressures. The activation energy also changed with increasing pressure by an amount equal to the heat of adsorption of n-hexane in ZSM-5, going from 90 to 170 kJ/mol. The selectivity for C-7+ products varied only with temperature and conversion.
Co-reporter:Sounak Roy, Giannis Mpourmpakis, Do-Young Hong, Dionisios G. Vlachos, A. Bhan, and R. J. Gorte
ACS Catalysis 2012 Volume 2(Issue 9) pp:1846
Publication Date(Web):July 19, 2012
DOI:10.1021/cs300176d
The acid sites on γ-Al2O3 were characterized using FTIR spectroscopy of adsorbed pyridine and temperature programmed desorption (TPD) of 2-propanamine, ethanol, 1-propanol, 2-propanol, and 2-methyl-2-propanol, together with density functional theory (DFT) calculations. Following room-temperature adsorption and evacuation, the surface coverages of the adsorbed alcohols were between 2 and 3.2 × 1018 molecules/m2. For each of the adsorbed alcohols, reaction to olefin and water products occurred in a narrow peak that indicated reaction is a first-order process with a well-defined activation energy, which in turn depended strongly on the particular alcohol. DFT calculations on an Al8O12 cluster are in excellent agreement with the experimental observations and show that the transition states for dehydration had carbenium-ion character. The carbenium ion stability in terms of proton affinity (of alkenes) matches well with the activation energy of the dehydration reaction. Adsorption of water on the γ-Al2O3, followed by evacuation at 373 K, demonstrated that water simply blocks sites for the alcohols without affecting the reaction activation energy. There was no evidence for Brønsted sites on the γ-Al2O3 based on FTIR of pyridine or TPD of 2-propanamine.Keywords: acid sites; alcohol dehydration; alumina; DFT; reaction mechanism; TPD-TGA;
Co-reporter:Lawrence Adijanto, Venu Balaji Padmanabhan, Rainer Küngas, Raymond J. Gorte and John M. Vohs  
Journal of Materials Chemistry A 2012 vol. 22(Issue 22) pp:11396-11402
Publication Date(Web):27 Apr 2012
DOI:10.1039/C2JM31774E
The physical and electrochemical properties of cerium vandates in which a portion of the cerium cations have been substituted with transition metals (Ce1−xTMxVO4−0.5x, TM = Ni, Co, Cu) were investigated and their suitability for use in solid oxide fuel cell (SOFC) anodes was assessed. Similar to other transition metal doped perovskites, the metals were found to move out of and into the oxide lattice in response to exposure to reducing and oxidizing conditions at elevated temperatures. This process produces nanoparticle metal catalysts that decorate the surface of the conductive cerium vanadate. Solid oxide fuel cells (SOFC) with Ce1−xTMxVO3–YSZ composite anodes exhibited high electrochemical activity. It was also demonstrated that doping with the alkaline earth ions, Ca2+ and Sr2+ enhances the electronic conductivity of the vanadate and Ce0.7Sr0.1Ni0.2VO3–YSZ composite SOFC anodes were found to have both high electrochemical activity and unusually high redox stability.
Co-reporter:Kevin Bakhmutsky;Dr. Noah L. Wieder;Matteo Cargnello;Benjamin Galloway;Dr. Paolo Fornasiero;Dr. Raymond J. Gorte
ChemSusChem 2012 Volume 5( Issue 1) pp:140-148
Publication Date(Web):
DOI:10.1002/cssc.201100491

Abstract

A method, based on self assembly, for preparing core–shell nanostructures that are dispersible in organic solvents is demonstrated for Pd and Pt cores with CeO2, TiO2, and ZrO2 shells. Transmission electron microscopy (TEM) of these nanostructures confirmed the formation of distinct metal cores, approximately 2 nm in diameter, surrounded by amorphous oxide shells. Functional catalysts were prepared by dispersing the nanostructures onto an Al2O3 support; and vibrational spectra of adsorbed CO, together with adsorption uptakes, were used to demonstrate the accessibility of the metal core to CO and the porous nature of the oxide shell. Measurements of water-gas-shift (WGS) rates demonstrated that these catalysts exhibit activities similar to that of conventional supported catalysts despite having lower metal dispersions. Pd-based CeO2 and TiO2 core–shell catalysts exhibit significant transient deactivation, which is probably caused by a decrease in the exposed metal surface area due to the ease of reduction of the shells. Alternatively, Pt-based analogous core–shell catalysts do not exhibit such a transient decrease. Both Pd- and Pt-based ZrO2 core–shell catalysts deactivate at a significantly lower rate due to the less reducible nature of the ZrO2 shell.

Co-reporter:Rainer Küngas, Fred Bidrawn, Eyas Mahmoud, John M. Vohs, Raymond J. Gorte
Solid State Ionics 2012 Volume 225() pp:146-150
Publication Date(Web):4 October 2012
DOI:10.1016/j.ssi.2012.04.030
An analytical model has been developed and experimentally tested to determine the factors that lead to high overpotentials in composite solid oxide fuel cell (SOFC) cathodes. Results suggest that the performance of infiltrated, composite electrodes is limited by O2 adsorption and incorporation into the perovskite lattice. The impedance of cathodes prepared by infiltration of La0.8Sr0.2FeO3 (LSF) into porous yttria-stabilized zirconia (YSZ) depends strongly on the surface area of the perovskite phase and is independent of LSF film thickness. Model predictions about the effect of the microstructure and ionic conductivity of the porous electrolyte scaffold were also verified.Highlights► Analytical model of SOFC composite cathodes. ► Electrode performance is limited by perovskite surface area. ► Electrolyte surface area and ionic conductivity also affect cathode impedance.
Co-reporter:J. J. Delgado Jaén;M. Cargnello;K. Bakhmutsky;J. C. Hernández Garrido;T. Montini;J. J. Calvino Gámez;R. J. Gorte;P. Fornasiero
Science 2012 Volume 337(Issue 6095) pp:713-717
Publication Date(Web):10 Aug 2012
DOI:10.1126/science.1222887

Addressing a Burning Issue

Complete combustion of methane is required in order to avoid the unproductive emission of this greenhouse gas into the atmosphere. Palladium catalysts can help to promote complete combustion, but high-temperature operating conditions also promote aggregation of catalyst particles (“sintering”) that lowers their surface area and overall activity. Cargnello et al. (p. 713; see the Perspective by Farrauto) report that cerium oxide–coated Pd catalyst particles could be fully dispersed on an alumina surface prepared with a hydrophobic coating. This treatment resisted Pd sintering up to temperatures of 800°C, and also enabled complete combustion of methane to occur at temperatures as low as 400°C.

Co-reporter:M. Cargnello;P. Fornasiero;R. J. Gorte
Catalysis Letters 2012 Volume 142( Issue 9) pp:1043-1048
Publication Date(Web):2012 September
DOI:10.1007/s10562-012-0883-4
The oxides used as supports for metal catalysts can be used to modify the catalyst properties. In this paper, we discuss three relatively new ways for optimizing the oxide–metal interactions and show examples where these methods have been used to improve catalytic performance. Opportunities still exist for using each of these approaches to produce materials with improved catalytic performance.
Co-reporter:Kevin Bakhmutsky;Jasmin Imran Alsous
Catalysis Letters 2012 Volume 142( Issue 5) pp:578-581
Publication Date(Web):2012 May
DOI:10.1007/s10562-012-0808-2
The redox properties of a vanadium phosphorus oxide (VPO) catalyst with a V:P ratio of one were investigated using Coulometric Titration at 873 K. Equilibrium between (VO)2P2O7 and VOPO4 exists at a P(O2) of 3 × 10−4 atm, corresponding to ΔG of −60 kJ/mol O2. This value for VPO is significantly lower than that measured with other vanadium-containing catalysts that have been studied. Furthermore, compared to other vanadium catalysts, V+4 was stabilized against further reduction at lower P(O2). These redox thermodynamics may help to explain the unique catalytic properties of VPO catalysts for partial oxidation of butane to maleic anhydride.
Co-reporter:Abhimanyu Jayakumar, Rainer Küngas, Sounak Roy, Ashay Javadekar, Douglas J. Buttrey, John M. Vohs and Raymond J. Gorte  
Energy & Environmental Science 2011 vol. 4(Issue 10) pp:4133-4137
Publication Date(Web):11 Aug 2011
DOI:10.1039/C1EE01863A
The direct utilization of carbonaceous fuels is examined in a solid oxide fuel cell (SOFC) with a molten Sb anode at 973 K. It is demonstrated that the anode operates by oxidation of metallic Sb at the electrolyte interface, with the resulting Sb2O3 being reduced by the fuel in a separate step. Although the Nernst Potential for the Sb-Sb2O3 mixture is only 0.75 V, the electrode resistance associated with molten Sb is very low, approximately 0.06 Ωcm2, so that power densities greater than 350 mW cm−2 were achieved with an electrolyte-supported cell made from Sc-stabilized zirconia (ScSZ). Temperature programmed reaction measurements of Sb2O3 with sugar char, rice starch, carbon black, and graphite showed that the Sb2O3 is readily reduced by a range of carbonaceous solids at typical SOFC operating conditions. Finally, stable operation with a power density of 300 mW cm−2 at a potential of 0.5 V is demonstrated for operation on sugar char.
Co-reporter:Jong-Sung Park, Ian D. Hasson, Michael D. Gross, Chen Chen, J.M. Vohs, R.J. Gorte
Journal of Power Sources 2011 Volume 196(Issue 18) pp:7488-7494
Publication Date(Web):15 September 2011
DOI:10.1016/j.jpowsour.2011.05.028
Ceramic composites were prepared by infiltration of La0.7Sr0.3VO3.85 (LSV) into porous scaffolds of yttria-stabilized zirconia (YSZ) and tested for use as solid oxide fuel cell (SOFC) anodes. There was no evidence for solid-state reaction between LSV and YSZ at calcination temperatures up to 1273 K. For calcination at 973 K, LSV formed a continuous film over the YSZ. The LSV phase reduced easily upon heating in H2 to 973 K, with the reduction forming pores in the LSV and greatly increasing its surface area. The electrodes showed high electronic conductivity after reduction, with a 10-vol% LSV–YSZ composite exhibiting a conductivity of 2 S cm−1 at 973 K. In the absence of an added catalyst, the LSV–YSZ electrodes showed relatively poor performance; however, an electrode impedance of approximately 0.1 Ω cm2 was achieved at 973 K in humidified H2 following addition of 0.5 vol% Pd and 2.8 vol% ceria The LSV–YSZ composites were stable in CH4 but there was evidence for poisoning of the Pd catalyst by V following high-temperature oxidation.Highlights► Composite anode was prepared by infiltration of La0.7Sr0.3VO3.85 into porous YSZ. ► This anode has a sufficiently high electronic conductivity and reduces easily. ► The addition of a Pd/ceria catalyst decreases electrode impedances in both H2 and CH4 fuels.
Co-reporter:Lawrence Adijanto, Rainer Küngas, Jongsung Park, John M. Vohs, Raymond J. Gorte
International Journal of Hydrogen Energy 2011 Volume 36(Issue 24) pp:15722-15730
Publication Date(Web):December 2011
DOI:10.1016/j.ijhydene.2011.09.059
Several tungsten bronzes were investigated for use in solid oxide fuel cell (SOFC) anodes. Composite anodes were prepared by infiltration of the precursor salts into a porous yttria-stabilized zirconia (YSZ) scaffold to produce 40-wt% composites with bronze compositions of Na0.8NbyW1−yO3−δ (y = 0, 0.3, 0.7, and 1), K0.5WO3−δ, Cs0.2WO3−δ, and Rb0.2WO3−δ. XRD data showed that the bronze structures were formed following reduction in humidified H2 at 873 K but that the bronzes were partially reduced to metallic W above 1073 K. Composite conductivities as high as 130 S/cm were observed at 973 K for the Na0.8WO3−δ-YSZ composite but substitution of Nb significantly decreased the conductivity without increasing the temperature at which tungsten was reduced. The impedance of Na0.8WO3−δ-YSZ anodes in humidified H2 at 973 K was greater than 1.0 Ω cm2 but this decreased to approximately 0.3 Ω cm2 upon the addition of 1-wt% Pd for catalytic purposes. The possible use of anodes based on tungsten bronzes is discussed.Highlights► Infiltration procedures were used to prepare SOFC anodes from various tungsten bronzes. ► Bronze-YSZ composites showed conductivities as high as 130 S/cm at 973 K. ► The Na-W bronze was stable in humidified H2 below 1023 K but could be reduced to metallic W above 1073 K. ► As with other ceramic anodes, the addition of a catalyst was required to achieve low anode impedance.
Co-reporter:Noah L. Wieder ; Matteo Cargnello ; Kevin Bakhmutsky ; Tiziano Montini ; Paolo Fornasiero
The Journal of Physical Chemistry C 2011 Volume 115(Issue 4) pp:915-919
Publication Date(Web):June 21, 2010
DOI:10.1021/jp102965e
An alumina-supported, Pd@CeO2, core−shell catalyst having 1 wt % Pd and 9 wt % ceria was characterized for the water-gas-shift (WGS) reaction. Although the catalyst initially exhibited similar WGS rates to that of a conventional Pd/ceria catalyst at 623 K in 25 Torr each of CO and H2O, the Pd@CeO2 catalyst deactivated severely over the period of 1 h. The WGS activity of the Pd@CeO2 could be completely restored by mild oxidation, and oxygen-titration measurements showed that the ceria shell in the Pd@CeO2 catalyst was significantly reduced after being used for the WGS reaction. These observations are in sharp contrast to those found with a conventional Pd/ceria catalyst, for which the ceria remains almost fully oxidized under WGS conditions. CO adsorption measurements, using FTIR at room temperature and CO uptakes at 195 K, indicated that Pd in the oxidized Pd@CeO2 catalyst was accessible to CO, but adsorption was completely suppressed on the reduced catalyst. A model is presented to explain the results, which assumes that cracks and fissures in the oxidized ceria shell allow access to the Pd core but that reduction blocks access, either due to changes in the density of the ceria, which closes the fissures, or to coverage of the metal surface with ceria.
Co-reporter:F. Bidrawn, G. Kim, N. Aramrueang, J.M. Vohs, R.J. Gorte
Journal of Power Sources 2010 Volume 195(Issue 3) pp:720-728
Publication Date(Web):1 February 2010
DOI:10.1016/j.jpowsour.2009.08.034
The influence of various infiltrated dopants on the performance of solid oxide fuel cell (SOFC) cathodes was examined. The cathodes were prepared by infiltration of nitrate salts into porous yttria-stabilized zirconia (YSZ) to produce composites with 40-wt% of either La0.8Sr0.2FeO3 (LSF) or La0.8Sr0.2MnO3 (LSM) and were then calcined to either 1123 or 1373 K. The addition of dopants had little influence on the 1123-K composite electrodes but all dopants tested improved the performance of the 1373-K composites. With 1373-K, LSF–YSZ electrodes, the open-circuit impedances decreased dramatically following the addition of 10-wt% YSZ, 0.5-wt% Pd, 10-wt% Ce0.8Sm0.2O1.9 (SDC), 10-wt% CaO, and 10-wt% K2O. Similarly, the 1373-K, LSM–YSZ electrodes were enhanced by the addition of 10-wt% CeO2, 1-wt% Pd, and 10-wt% YSZ. Since the improved performance was close to that of the corresponding LSF–YSZ and LSM–YSZ electrodes that had been calcined to only 1123 K, it is suggested that the improved performance is related to structural changes in the electrode, rather than to improved catalytic properties or ionic conductivity.
Co-reporter:A. Jayakumar, J. M. Vohs, and R. J. Gorte
Industrial & Engineering Chemistry Research 2010 Volume 49(Issue 21) pp:10237-10241
Publication Date(Web):May 26, 2010
DOI:10.1021/ie100457t
Molten In, Pb, and Sb were examined as anodes in solid oxide fuel cells (SOFC) that operate between 973 and 1173 K. The results for these metals were compared with those reported previously for molten Sn electrodes. Cells were operated under “battery” conditions, with dry He or N2 flow in the anode compartment, to characterize the electrochemical oxidation of the metals at the yttria-stabilized zirconia (YSZ)-electrolyte interface. In most cases, the open-circuit voltages (OCVs) were close to that based on equilibrium between the metals and their oxides. With Sn and In, the cell impedances increased dramatically at all temperatures after drawing current due to formation of insulating, oxide barriers at the electrolyte interface. Similar results were observed for Pb at 973 and 1073 K, but the impedance remained low even after PbO formation at 1173 K because this is above the melting temperature of PbO. Similarly, the impedances of molten Sb electrodes at 973 K were low and unaffected by current flow because of the low melting temperature of Sb2O3. The potential of using molten-metal electrodes for direct-carbon fuel cells and for energy-storage systems is discussed.
Co-reporter:John M. Vohs
Advanced Materials 2009 Volume 21( Issue 9) pp:943-956
Publication Date(Web):
DOI:10.1002/adma.200802428

Abstract

Improved cathodes are required for low-temperature operation of solid-oxide fuel cells (SOFCs). Recent work has shown that electrode fabrication and modification by infiltration of active components into a porous scaffold can result in outstanding electrochemical performance. In this paper we review the literature on this new approach for cathode preparation and discuss the insights that this work has provided for understanding the relationships between the materials properties, electrochemical performance, and electrode stability.

Co-reporter:Shiwoo Lee, M. Bevilacqua, P. Fornasiero, J.M. Vohs, R.J. Gorte
Journal of Power Sources 2009 Volume 193(Issue 2) pp:747-753
Publication Date(Web):5 September 2009
DOI:10.1016/j.jpowsour.2009.04.046
Co-reporter:Kevin Bakhmutsky;Gong Zhou;Steven Timothy
Catalysis Letters 2009 Volume 129( Issue 1-2) pp:61-65
Publication Date(Web):2009 April
DOI:10.1007/s10562-009-9882-5
Reaction rates for the water–gas-shift (WGS) reaction were measured on catalysts with 1-wt% Pd supported on CeO2, Ce0.5Pr0.5O2−x and PrOx in order to determine whether the weakly bound oxygen associated with Pr could enhance reaction rates. However, differential rates in 25 Torr of both CO and H2O showed that the activity of Pr-containing catalysts were much lower. Measurements of the oxygen content of these samples after reduction in dry H2 at 873 K, after reoxidation in steam at 873 K, and following exposure of the catalysts to WGS conditions at 873 K demonstrate that ceria is easily reoxidized by steam and remains oxidized under WGS conditions, while the loosely bound oxygen associated with praseodymia or ceria–praseodymia is lost under WGS conditions and cannot be restored by oxidation in steam. These results can be understood by comparing the equilibrium redox properties of the support materials to the typical P(O2) experienced under WGS conditions.
Co-reporter:Guntae Kim, John M. Vohs and Raymond J. Gorte  
Journal of Materials Chemistry A 2008 vol. 18(Issue 20) pp:2386-2390
Publication Date(Web):11 Mar 2008
DOI:10.1039/B718931A
Composites prepared by infiltration of 50- wt% ceria into porous YSZ were investigated for use as H2–H2O electrodes for solid oxide electrolyzers (SOE) or fuel cells (SOFC). Cells prepared from these composites showed excellent performance, with SOFC power densities as high as 1.1 W cm−2 at 1073 K. Further investigations into the electrodes showed that they had significantly higher conductivities than would be expect for a material that was only 35 vol% ceria, as high as 0.25 S cm−1 at 1073 in 3% H2O–97% H2 mixtures. An investigation into the thermodynamic redox properties of the composite using coulometric titration at 973 K indicated that the ceria in the composite remained significantly reduced to higher P(O2) compared to pure ceria, probably due to interactions at the ceria–YSZ interface.
Co-reporter:Parag R. Shah;John M. Vohs
Catalysis Letters 2008 Volume 125( Issue 1-2) pp:
Publication Date(Web):2008 September
DOI:10.1007/s10562-008-9539-9
Redox isotherms were measured for zirconia-supported vanadia between 10−2 and 10−28 atm at 748 K for two vanadia loadings, 2.9 and 5.8 V/nm2, corresponding to isolated VO4 species and monolayer, polymeric vanadates. The catalyst with isolated VO4 species, which is expected to have predominantly V–O–Zr linkages, had a redox isotherm that showed a well-defined step corresponding to one oxygen per V. By contrast, the redox isotherm for the catalyst with polymeric vanadates changed more gradually with \( \hbox{P}_{{\rm O}_2} \) and the change in the oxygen stoichiometry corresponded to 0.85 O/V. Comparison of these results to the redox isotherms for bulk vanadates suggests that oxidation of the isolated vanadates proceeds by a direct transition from V+3 ↔ V+5, while transitions from V+3 ↔ V+4 and V+4 ↔ V+5 are possible with the polyvanadates. Rate measurements for methanol and propane oxidation over the two supported vanadia catalysts and several bulk vanadates showed that specific rates for each reaction were similar on all of the samples, suggesting that that the V–O bond strength does not affect the rate determining step of these reactions.
Co-reporter:M. D. Gross, J. M. Vohs and R. J. Gorte  
Journal of Materials Chemistry A 2007 vol. 17(Issue 30) pp:3071-3077
Publication Date(Web):02 May 2007
DOI:10.1039/B702633A
There would be significant advantages to having anodes for solid oxide fuel cells (SOFCs) that were capable of directly utilizing hydrocarbon fuels. Because conventional Ni-based anodes catalyze the formation of carbon fibers, new anode compositions are required for this application, but most of the materials that have been proposed exhibit either limited thermal stability or poor electrochemical activity. In this paper, we will describe two strategies for the development of new anodes with improved performance. The first strategy involves the use of bimetallic compositions with layered microstructures. In the bimetallic anodes, one metal is used for thermal stability while the other provides the required carbon tolerance. The second strategy involves separating the anode into two layers: a thin functional layer for electrocatalysis and a thicker conduction layer for current collection. With this approach, the functional layer can be optimized for catalytic activity and, if it is thin enough, requires minimal conductivity. Examples are shown for each of these approaches and possible future directions are outlined.
Co-reporter:Taeyoon Kim, Kipyung Ahn, John M. Vohs, Raymond J. Gorte
Journal of Power Sources 2007 Volume 164(Issue 1) pp:42-48
Publication Date(Web):10 January 2007
DOI:10.1016/j.jpowsour.2006.09.101
The performance and stability of Cu-ceria-YSZ (yttria-stabilized zirconia) and carbon-ceria-YSZ, solid-oxide-fuel-cell (SOFC) anodes were examined in neat (100%) methanol at 973 K and compared to the performance of the same anodes in dry H2. The presence of Cu catalyzed the decomposition of methanol, so that the initial performance of cells with Cu-ceria-YSZ anodes was similar to CO and H2. However, with carbon-ceria-YSZ anodes, the open-circuit voltage was significantly higher and the reaction over-potential significantly lower in methanol than in H2, suggesting that methanol is a more effective reductant of the anode three-phase boundary region. Carbon-ceria-YSZ anodes were found to undergo rapid and irreversible deactivation in methanol. Steady-state rates of methanol decomposition over ceria-YSZ were found to undergo a similar deactivation as the carbon-ceria anodes. Although no evidence for carbon deposition was observed with methanol at 973 K, the addition of steam was found to partially stabilize both anode and catalyst performance. Scanning electron microscopy (SEM) of ceria particles in YSZ showed a large change in the morphology of the ceria particles when the samples were heated in methanol, while negligible changes were observed when heating in H2. It is suggested that the results with methanol can be explained as resulting from the very low P(O2) that is effectively produced by having methanol in contact with ceria.
Co-reporter:Wensheng Wang;John M. Vohs
Topics in Catalysis 2007 Volume 46( Issue 3-4) pp:380-385
Publication Date(Web):2007 December
DOI:10.1007/s11244-007-9005-8
Porous composite anodes consisting of a yttria-stabilized zirconia (YSZ) backbone that was impregnated with CeO2 and various amounts of metallic components including Cu, Co and Pd were fabricated. The performance of these anodes was then tested in a solid oxide water electrolysis cell under conditions where the anode was exposed to the reducing gasses H2, CH4 and CO. The reducing gasses were used to decrease the electrochemical potential of the cell and increase overall efficiency. The results of this study show that Cu–CeO2–YSZ anodes have low catalytic activity for the oxidation of CO and CH4 and are not very effective in lowering the cell potential while operating in the reducing gas assisted mode. The addition of Co to the Cu–CeO2–YSZ anode resulted in a modest increase in the catalytic activity and enhanced the thermal stability of the anode. A Pd–C–CeO2–YSZ anode was found to have the highest catalytic activity of those tested and gave the largest reductions in the operating potential of the solid oxide electrolysis cell.
Co-reporter:O Kresnawahjuesa, R.J Gorte, David White
Journal of Molecular Catalysis A: Chemical 2004 Volume 212(1–2) pp:309-314
Publication Date(Web):2 April 2004
DOI:10.1016/j.molcata.2003.11.015
We have studied the vapor-phase reaction of acetic acid with propene over H-[Al]ZSM-5 and H-[Fe]ZSM-5 molecular sieves between 425 and 600 K, for acetic acid partial pressures of 0.033–0.066 Bar, with propene:acetic acid ratios between 1 and 4. Reasonable conversions were obtained above 450 K. Both H-[Fe]ZSM-5 and H-[Al]ZSM-5 showed high activities at 450 K, with selectivities to propyl acetates of ∼90% using a propene:acetic acid ratio of 2 and ketones formed by dehydration of the acetates making up most of the remaining products. The reaction rate was completely stable at 450 K for at least 20 h, and the product distribution was insensitive to the reactant feed ratio for a propene:acetic acid ratio above 2. On H-[Fe]ZSM-5, dehydration of the acetates became increasingly important at higher temperatures, with the selectivity to ketones approaching 80% at 525 K. At still higher temperatures, reaction pathways that did not involve propyl acetates became important. The high selectivity for forming propyl acetates and the absence of olefin oligomerization is believed to result from having the acid sites occupied (saturated) by acetic acid. Finally, the acid-site density measured on H-[Fe]ZSM-5 after weeks of catalyst testing remained the same as the initial site density, showing that this material has sufficient stability for fine-chemicals synthesis.Graphic
Co-reporter:R.J. Gorte, H. Kim, J.M. Vohs
Journal of Power Sources 2002 Volume 106(1–2) pp:10-15
Publication Date(Web):1 April 2002
DOI:10.1016/S0378-7753(01)01021-7
This paper describes recent developments in solid-oxide fuel cells (SOFC) that use Cu-based cermets as the anode for direct oxidation of hydrocarbon fuels, including liquids such as gasoline, to generate electrical power without the need for first reforming that fuel to H2. Cu–YSZ cermets were found to be stable in hydrocarbon environments, but exhibited low performance for direct oxidation. Reasonable power densities could only be achieved with the addition of a catalytic oxide, like ceria, with the Cu cermet. Electrochemical oxidation studies demonstrated that the initial products for reaction depend on the catalytic oxide. Finally, the effect of sulfur impurities in the fuel is discussed.
Co-reporter:Hyuk Kim, John M. Vohs and Raymond J. Gorte  
Chemical Communications 2001 (Issue 22) pp:2334-2335
Publication Date(Web):25 Oct 2001
DOI:10.1039/B105713H
Solid-oxide fuel cells with Cu–ceria anodes are shown to provide stable power generation through the direct oxidation of hydrocarbon fuels having sulfur levels similar to that in gasoline and can be regenerated by steam after being poisoned with higher sulfur levels.
Co-reporter:Seungdoo Park;John M. Vohs
Nature 2000 404(6775) pp:265-267
Publication Date(Web):2000-03-16
DOI:10.1038/35005040
The direct electrochemical oxidation of dry hydrocarbon fuels to generate electrical power has the potential to accelerate substantially the use of fuel cells in transportation and distributed-power applications1. Most fuel-cell research has involved the use of hydrogen as the fuel, although the practical generation and storage of hydrogen remains an important technological hurdle2. Methane has been successfully oxidized electrochemically3, 4, 5, 6, but the susceptibility to carbon formation from other hydrocarbons that may be present or poor power densities have prevented the application of this simple fuel in practical applications1. Here we report the direct, electrochemical oxidation of various hydrocarbons (methane, ethane, 1-butene, n-butane and toluene) using a solid-oxide fuel cell at 973 and 1,073 K with a composite anode of copper and ceria (or samaria-doped ceria). We demonstrate that the final products of the oxidation are CO2 and water, and that reasonable power densities can be achieved. The observation that a solid-oxide fuel cell can be operated on dry hydrocarbons, including liquid fuels, without reforming, suggests that this type of fuel cell could provide an alternative to hydrogen-based fuel-cell technologies.
Co-reporter:Gong Zhou, Jonathan Hanson, Raymond J. Gorte
Applied Catalysis A: General (8 February 2008) Volume 335(Issue 2) pp:153-158
Publication Date(Web):8 February 2008
DOI:10.1016/j.apcata.2007.11.011
Co-reporter:Tzia Ming Onn, Matteo Monai, Sheng Dai, Lisandra Arroyo-Ramirez, Shuyi Zhang, Xiaoqing Pan, George W. Graham, Paolo Fornasiero, Raymond J. Gorte
Applied Catalysis A: General (25 March 2017) Volume 534() pp:
Publication Date(Web):25 March 2017
DOI:10.1016/j.apcata.2017.01.025
•High-surface-area Fe2O3 film was prepared by Atomic Layer Deposition on Al2O3.•Fe2O3 grows as a uniform, dense layer over the Al2O3.•Pd-impregnated on the ALD-modified Al2O3 shows high water-gas-shift rates.•The ALD-prepared Fe2O3 shows improved thermal stability compared to bulk Fe2O3.High-surface-area iron oxides were prepared by Atomic Layer Deposition (ALD) on 130-m2/g γ-Al2O3 for use as a catalyst support. Measurements of the sample mass, surface area, and pore-size distribution as a function of the number of ferrocene-O2 ALD cycles at 623 K suggested that the iron oxide grew as a dense, conformal film with a growth rate similar to 0.016-nm per cycle. While films with 20 ALD cycles (20Fe2O3-Al2O3, 0.25 g Fe2O3/g Al2O3) were difficult to distinguish by HAADF STEM, EDS mapping indicated the Al2O3 was uniformly coated. Raman Spectroscopy showed the films were in the form of Fe2O3; but XRD measurements on samples with as many as 100 ALD cycles (100Fe2O3-Al2O3, 0.84 g Fe2O3/g Al2O3) showed no evidence for crystalline iron-oxide phases, even after calcination at 1073 K. Specific rates for the water-gas-shift (WGS) reaction on the ALD-coated samples were significantly lower than those on bulk Fe2O3. However, addition of 1 wt.% Pd to Fe2O3/Al2O3 supports prepared by ALD exhibited specific rates that were much higher than that observed when 1 wt.% Pd was added to Fe2O3/Al2O3 prepared by conventional impregnation of Fe salts, suggesting more uniform contact between the Pd and FeOx phases on samples prepared by ALD.
Co-reporter:Jing Luo, Balaaji V. Bhaskar, Yu-Hao Yeh, Raymond J. Gorte
Applied Catalysis A: General (20 May 2014) Volume 478() pp:228-233
Publication Date(Web):20 May 2014
DOI:10.1016/j.apcata.2014.04.010
Co-reporter:P.R. Shah, I. Baldychev, J.M. Vohs, R.J. Gorte
Applied Catalysis A: General (20 June 2009) Volume 361(Issues 1–2) pp:13-17
Publication Date(Web):20 June 2009
DOI:10.1016/j.apcata.2009.03.036
Co-reporter:Jingye Yu, Shiyu Zhu, Paul J. Dauenhauer, Hong Je Cho, Wei Fan and R. J. Gorte
Catalysis Science & Technology (2011-Present) 2016 - vol. 6(Issue 14) pp:NaN5736-5736
Publication Date(Web):2016/04/13
DOI:10.1039/C6CY00501B
The adsorption and reaction properties of H-BEA, SnBEA, ZrBEA and siliceous BEA were examined to understand the reaction of 2,5-dimethylfuran (DMF) with ethylene to form p-xylene. Temperature-programmed desorption (TPD) of diethyl ether, DMF, 2,5-hexanedione and p-xylene on each of the zeolites demonstrated that the Brønsted sites in H-BEA are more reactive than the Lewis sites in SnBEA and ZrBEA and tend to promote the oligomerization of DMF and 2,5-hexanedione, even at 295 K; however, the adsorbed 2,5-hexanedione is converted to DMF at both Lewis- and Brønsted-acid sites. H-BEA, SnBEA and ZrBEA all catalyzed the reaction to p-xylene with high selectivity in a continuous-flow reactor, with all three catalysts showing rates that were first order in both DMF and ethylene. H-BEA was found to deactivate rapidly due to coking, while ZrBEA and SnBEA were both stable. The implications of these results for practical applications are discussed.
Co-reporter:Lawrence Adijanto, Venu Balaji Padmanabhan, Rainer Küngas, Raymond J. Gorte and John M. Vohs
Journal of Materials Chemistry A 2012 - vol. 22(Issue 22) pp:NaN11402-11402
Publication Date(Web):2012/04/27
DOI:10.1039/C2JM31774E
The physical and electrochemical properties of cerium vandates in which a portion of the cerium cations have been substituted with transition metals (Ce1−xTMxVO4−0.5x, TM = Ni, Co, Cu) were investigated and their suitability for use in solid oxide fuel cell (SOFC) anodes was assessed. Similar to other transition metal doped perovskites, the metals were found to move out of and into the oxide lattice in response to exposure to reducing and oxidizing conditions at elevated temperatures. This process produces nanoparticle metal catalysts that decorate the surface of the conductive cerium vanadate. Solid oxide fuel cells (SOFC) with Ce1−xTMxVO3–YSZ composite anodes exhibited high electrochemical activity. It was also demonstrated that doping with the alkaline earth ions, Ca2+ and Sr2+ enhances the electronic conductivity of the vanadate and Ce0.7Sr0.1Ni0.2VO3–YSZ composite SOFC anodes were found to have both high electrochemical activity and unusually high redox stability.
Co-reporter:Guntae Kim, John M. Vohs and Raymond J. Gorte
Journal of Materials Chemistry A 2008 - vol. 18(Issue 20) pp:NaN2390-2390
Publication Date(Web):2008/03/11
DOI:10.1039/B718931A
Composites prepared by infiltration of 50- wt% ceria into porous YSZ were investigated for use as H2–H2O electrodes for solid oxide electrolyzers (SOE) or fuel cells (SOFC). Cells prepared from these composites showed excellent performance, with SOFC power densities as high as 1.1 W cm−2 at 1073 K. Further investigations into the electrodes showed that they had significantly higher conductivities than would be expect for a material that was only 35 vol% ceria, as high as 0.25 S cm−1 at 1073 in 3% H2O–97% H2 mixtures. An investigation into the thermodynamic redox properties of the composite using coulometric titration at 973 K indicated that the ceria in the composite remained significantly reduced to higher P(O2) compared to pure ceria, probably due to interactions at the ceria–YSZ interface.
Co-reporter:Jing Luo, Jingye Yu, Raymond J. Gorte, Eyas Mahmoud, Dionisios G. Vlachos and Michael A. Smith
Catalysis Science & Technology (2011-Present) 2014 - vol. 4(Issue 9) pp:NaN3081-3081
Publication Date(Web):2014/06/02
DOI:10.1039/C4CY00563E
The liquid-phase (69 bar) reaction of 5-hydroxymethylfurfural (HMF) with 2-propanol for production of furanyl ethers was studied at 413 and 453 K over a series of oxide catalysts, including γ-Al2O3, ZrO2, TiO2, Al2O3/SBA-15, ZrO2/SBA-15, TiO2/SBA-15, H-BEA, and Sn-BEA. The acidity of each of the catalysts was first characterized for Brønsted sites using TPD-TGA of 2-propanamine and for Lewis sites using TPD-TGA of 1-propanol. Catalysts with strong Brønsted acidity (H-BEA and Al2O3/SBA-15) formed 5-[(1-methylethoxy)methyl]furfural with high selectivities, while materials with Lewis acidity (γ-Al2O3, ZrO2, TiO2, and Sn-BEA) or weak Brønsted acidity (ZrO2/SBA-15 and TiO2/SBA-15) were active for transfer hydrogenation from the alcohol to HMF to produce 2,5-bis(hydroxymethyl)furan, with subsequent reactions to the mono- or di-ethers. Each of the catalysts was stable under the flow-reactor conditions but the selectivities varied with the particular oxide being investigated.
Co-reporter:M. D. Gross, J. M. Vohs and R. J. Gorte
Journal of Materials Chemistry A 2007 - vol. 17(Issue 30) pp:NaN3077-3077
Publication Date(Web):2007/05/02
DOI:10.1039/B702633A
There would be significant advantages to having anodes for solid oxide fuel cells (SOFCs) that were capable of directly utilizing hydrocarbon fuels. Because conventional Ni-based anodes catalyze the formation of carbon fibers, new anode compositions are required for this application, but most of the materials that have been proposed exhibit either limited thermal stability or poor electrochemical activity. In this paper, we will describe two strategies for the development of new anodes with improved performance. The first strategy involves the use of bimetallic compositions with layered microstructures. In the bimetallic anodes, one metal is used for thermal stability while the other provides the required carbon tolerance. The second strategy involves separating the anode into two layers: a thin functional layer for electrocatalysis and a thicker conduction layer for current collection. With this approach, the functional layer can be optimized for catalytic activity and, if it is thin enough, requires minimal conductivity. Examples are shown for each of these approaches and possible future directions are outlined.
Pentanedione
Platinum(II) acetylacetonate
Nickel, compd. with platinum (1:1)
Cobalt, compd. with platinum (1:3)
Furan, 2-(dipropoxymethyl)-
Furan, 2,5-bis(propoxymethyl)-
Hexane, 2,5-dipropoxy-
TETRAAMMINEPLATINUM DINITRATE
2-Furanmethanol, 5-(propoxymethyl)-