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YearTitleAuthorsDOIReferenceKeywordsAbstract
2024Enhanced catalytic performance of B-doped SiC supported Ni catalysts for the hydrogenation of nitroarenesJi-Xiao Zhao, Dan Yao, Lei Li, Jia-Hang Li, Zhi-Feng Jiao, Xiang-Yun Guo10.1016/j.apcata.2024.119726Applied Catalysis A: General
Volume 678, 25 May 2024, 119726
Ni/SiC catalysts
B doping
Hydrogenation of nitroarenes
SiC and B-doped SiC were prepared and employed to support Ni components for the catalytic hydrogenation of nitroarenes. The B-doping of SiC evidently improved the catalytic activity of Ni/SiC, and the activity of Ni/SiCB0.5 catalyst was 2.4 times higher than that of undoped Ni/SiC. Further investigations revealed that the incorporation of B substituted some Si atoms in SiC lattice and thus produced carbon vacancies. These vacancies will result in a heterogeneous distribution of surface charges on SiC, thereby enhancing the adsorption and activation of nitroarenes on the support surface. In addition, the carbon vacancies can also act as donor centers for capturing dissociated hydrogen species, thus enhancing the hydrogen spillover from Ni to SiC surface.
2024Preparation of Co/SiC catalyst and its catalytic activity for ammonia decomposition to produce hydrogenRongji Xu, Fengxiang Yin, Jie Zhang, Guoru Li, Gideon Kofie, Yuhang Tan, Biaohua Chen10.1016/j.cattod.2024.114774Volume 437, 1 July 2024, 114774Co Catalyst
Hydrogen generation rate
Ammonia decomposition
SiC
SiC was first synthesized using the sol-gel method and subsequent carbothermal reduction method, then xCo/SiC-700 and 30%Co/SiC-T catalysts were prepared by hydrothermal method and thermal treatment. The structure of the catalysts was characterized by XRD, SEM/TEM, XPS, H2-TPR, CO2-TPD, etc. Their catalytic activities for ammonia decomposition to produce hydrogen were investigated in a fixed-bed reactor. The results showed that the synthesized SiC had a high specific surface area and could evenly disperse Co3O4 nanoparticles, which increased the exposure of active sites and improved the adsorption capacity on the catalyst surface. N2-TPD indicates that 30%Co/SiC-700 has a high N2 adsorption capacity, effectively preventing hydrogen reduction of Co3O4 nanoparticles in the catalyst during ammonia decomposition. CO-TPD shows that Co has the best dispersion on 30%Co/SiC-700 catalyst. CO2-TPD shows the higher the catalyst's basicity, the stronger ammonia's decomposition ability. Among the synthesized catalysts, 30% Co/SiC-700 showed the best catalytic activity for ammonia decomposition, with the ammonia conversion of 78.3% and hydrogen production of 25.0 mmol H2 gcat−1 min−1 at 550 °C under 30,000 mL gcat−1 h−1.
2024Natural catalysis-based clean hydrogen production from shale oil: An in-situ conversion enabled by electromagnetic heatingKeju Yan, Baizheng An, Qingwang Yuan10.1016/j.ijhydene.2024.03.078Volume 62, 10 April 2024, Pages 1245-1257In-situ hydrogen generation
Shale oil
Electromagnetic heating
Natural catalysis
Thermal runaway
Employing electromagnetic(EM)-assisted catalytic heating to produce hydrogen (H2) directly from petroleum reservoirs is an emerging technology for decarbonizing fossil fuel industry. Transforming hydrocarbons to clean H2 in situ will enable pure hydrogen extraction to surface while simultaneously sequestering carbon underground with the assistance of downhole hydrogen membrane separation technology. Here, we aim to characterize the role of shale rocks in enhancing EM heating and catalyzing shale oil conversion to hydrogen as natural catalysts under EM irradiation. Flow-through experiments are well designed and conducted in a customized microwave reactor system. We also identified for the first time that shale rocks exhibit a “thermal runaway” (TR) phenomenon which occurs at a temperature of 280 °C. After TR happens, the energy needed for heating shale samples to a high enough temperature is significantly reduced under EM irradiation. Further, we identified that metal-rich minerals in shale rocks play an evident natural catalytic effect on shale oil conversion to hydrogen. As a result, hydrogen with a percentage of 1 mol.% starts to be generated at a measured temperature of 253–421 °C in the presence of shale rocks and is a dominant gas in the generated gas products at high temperatures. The highest production rate and concentration of H2 gas are 178 sccm and 77 mol.% from the conversion of 0.4 g of shale oil, respectively. Importantly, CO2 generated during the process is negligible. This work lays a foundation for leveraging the abundant shale rocks and their natural catalytic effect for more efficient, cost-effective, in-situ hydrogen production directly from shale reservoir via the EM-assisted catalytic heating technology we recently proposed.
2024Microwave-Assisted dry reforming of toluene as a model tar compound using low-cost iron catalyst for syngas clean-upXinwei Bai, Ashraf Abedin, Anitha Shankara Linge Gowda, Victor Abdelsayed, Pranjali Muley10.1016/j.fuel.2024.131843Volume 370, 15 August 2024, 131843Tar Reforming
Dry reforming
Microwave Reactor
Syngas Cleanup
Gasification of waste feedstock such as biomass, waste plastics suffers from high tar yields during hydrogen-rich syngas production. The presence of tars result in lower quality syngas, lower syngas yields, reactor blockage, reactor down time, and costly maintenance. Therefore, removal of tar from syngas during gasification is essential. Catalytic reforming of tars via in-situ syngas cleanup is an effective way of mitigating tars. This work explores the possibility of microwave-assisted catalytic dry reforming of tars for syngas production. Due to its chemical complexity, toluene, which is one of the main tar constituents, could be used as a model tar compound. Toluene dry reforming was studied using the Fe/Al2O3 catalyst under CO2 under the temperature range of 400–700 ℃. The toluene reforming reaction was conducted using microwave and conventional thermal reactors. Under microwave irradiation, CO2 and toluene conversions are boosted to 80% at 500 ℃. Hydrogen and carbon monoxide yields were approximately five times and ten times higher in the microwave reactor at 500 ℃, respectively, compared to the productions obtained in the conventional fixed-bed reactor at 700 ℃. Filamentous carbon was also produced as a valuable side product to improve the economy of this process and such value-added carbon was only observed in the microwave reactor. Three reaction pathways were observed during microwave reaction: the toluene decomposition produces an initial hydrogen and carbon deposit on the catalyst; the formation of methane and benzene suggests toluene hydrodemethylation as a secondary reaction; and toluene hydrogenolysis forms light alkanes such as methane, and through reforming reaction under CO2 to syngas.
2018Making the Most of Precious Metal Nanoparticles in the Purification of Industrial Wastewater by Catalytic Wet Air Oxidation
Revealing synergy between platinum and catalyst support
Korrin Saunders, Dafydd Davies, Stan Golunski, Peter Johnston, Pawel Plucinski10.1595/205651318X15299289846952Applied Catalysis A: General
Volume 676, 25 April 2024, 119637
Catalytic Wet Air Oxidation
Phenol
hydrophobic catalyst
Platinum on SiC supports
The aim of catalytic wet air oxidation is to use air to remove organic contaminants from wastewater through their complete oxidation, without having to vaporise the water. To date, the widespread exploitation of this process has been held back by the low activity of available catalysts, which means that it has to be operated at above-atmospheric pressure in order to keep the water in the liquid phase at the elevated temperatures required to achieve complete oxidation. Here we present an overview of an ongoing study examining the key requirements of both the active phase and the support material in precious metal catalysts for wet air oxidation, using phenol as the model contaminant. The major outcome to date is that the results reveal a synergy between platinum and hydrophobic support materials, which is not apparent when the active phase is ruthenium.
2023Boosting the selectivity of Pt catalysts for cinnamaldehyde
hydrogenation to cinnamylalcohol by surface oxidation of SiC support
Lei Li, Zhi-Feng Jiao, Ji-Xiao Zhao, Dan Yao, Xiang Li, Xiang-Yun Guo10.1016/j.jcat.2023.06.018Catalysis Today
Volume 427, 1 February 2024, 114418
Pt/SiC-O
C=O selective adsorption
Cinnamaldehyde selective hydrogenation
The selective hydrogenation of cinnamaldehyde (CAL) is very important, but still remains challenging due to the coexistence of easily hydrogenated C=C and C=O bonds in CAL molecule. In this work, we report that employing partially oxidized SiC (SiC–O) as the support of Pt can evidently enhance the catalytic selectivity for the selective hydrogenation of C@O in CAL. Further investigations show that the partially oxidized SiC surface can change the adsorption mode of CAL and facilitate the selective adsorption of C=O in CAL. During the catalytic process, H2 was dissociated on Pt particles while CAL was mainly adsorbed and activated on the surface of support. The active H species generated on the Pt surface then spilled over to the support surface and reacted with the C=O bond activated by the support surface to selectively form cinnamylalcohol. The present work revealed an important cooperative catalysis of metal and SiC, which would be helpful to design and application of more SiC-based catalysts.
2024Exploring the feasibility of continuous CWAO of bisphenol A at near-ambient temperature and pressure through use of hydrophobic Pt catalystsKorrin Saunders, Stanislaw Golunski, Stuart H. Taylor, Pawel Plucinski, Albin Pintar, Gregor Zerjav10.1016/j.apcata.2024.119637Journal of Catalysis 425 (2023) 314-321Catalytic wet air oxidation
Wastewater treatment
Bisphenol A
Hydrophobic catalyst
Platinum on SiC supports
Hydrophobic Pt CWAO-catalysts can achieve complete removal of bisphenol A from a flow of contaminated water in a trickle-bed reactor at an operating temperature of 120°C, total air pressure of 8 bar and a liquid-hourly space velocity of 26.6 h−1. Although increasing the throughput of contaminated water while lowering the operating temperature results in bisphenol A conversions below 100%, these more demanding conditions allow structurally similar catalyst formulations to be differentiated from one another. At 60°C and 8 bar total pressure of air, 2%Pt supported on a SiC-TiC composite material has the highest initial activity from a group of three hydrophobic catalysts with similar surface areas and Pt particle diameters, but it begins to deactivate progressively after 15 hours on stream. This catalyst contains some localised hydrophilicity arising from the presence of surface TiO2, which forms when the exposed TiC component of the support material oxidises during catalyst preparation. At 80 °C and ambient air pressure, the activity is lower but there are no signs of deactivation during 24 hours on stream. The results are consistent with metallic platinum providing the active sites for CWAO of bisphenol A, with oxygen being directly activated from the gas phase at elevated pressures, but with dissolved oxygen also contributing to the reaction particularly at ambient air pressure. Continuous and irreversible deactivation, which occurs at air pressures ≥4 bar, appears to be associated with high occupancy of the active sites by adsorbed oxygen, resulting in leaching of platinum into the aqueous phase.
2018SO3 decomposition over CuO-CeO2 based catalysts in the sulfure iodine cycle for hydrogen productionLijian Wang, Yanqun Zhu, Hui Yang, Yong He, Jun Xia, Yanwei Zhang, Zhihua Wang10.1016/j.ijhydene.2018.06.056Mendeleaev Commun., 2023, 33, 832–835Hydrogen prodction
Sulfur-Iodine cycle
SO3 reduction
2016Influence of calcination temperature on CuOeCeO2/
SiC catalysts for SO3 decomposition in the
sulfureiodine cycle for hydrogen production
Hui Yang, Yanwei Zhang, Junhu Zhou, Zhihua Wang, Jianzhong Liu, Kefa Cen10.1016/j.ijhydene.2015.12.042International Journal of Hydrogen Energy
Volume 48, Issue 35, 26 April 2023, Pages 13068-13080
Hydrogen production
SO3 decomposition
CueCe/SiC catalyst
Calcination temperature
Oxidation
2020SO3 decomposition over β–SiC and SiO2 supported CuFe2O4: A stability and kinetic studySachin Tomar, Satyam Gangwar, Kishore Kondamudi, Sreedevi Upadhyayula10.1016/j.ijhydene.2020.05.177Catalysis Today
Volume 420, 1 August 2023, 114058
SO3 decomposition
kinetic studies
Catalyst
Characterization
Activity
Stability
CuFe2O4/β–SiC and CuFe2O4/SiO2 catalysts were prepared by wet impregnation method, following the high temperature solid state route and their catalytic performance is evaluated in the SO3 decomposition reaction of the Sulfur–Iodine (S–I) cycle for hydrogen production. The synthesized catalysts are characterized by XRD, FT–IR, TGA, XPS, N2–BET, TEM, HR–TEM, FESEM–EDS and elemental mapping. CuFe2O4/β–SiC catalyst shows higher activity and stability while sintering is observed in the spent CuFe2O4/SiO2 whose activity decreased during the reaction time on stream. Kinetic studies were performed over CuFe2O4/β-SiC in the temperature range of 800–900 °C using wide range of space time, 6.54–44.40 kg h kmol−1. A heterogeneous kinetic model was developed based on the product distribution and the reaction rates determined by the model fitted well with the experimental rates at different temperatures.
2023HMFI/SiC – a novel efficient catalyst for green hydrocarbon
production via bioisobutanol conversion
Alexey G. Dedov, Alexander A. Karavaev, Alexey S. Loktev, Petr V. Zemlianskii, Malika N. Vagapova, Konstantin I. Maslakov, Kirill A. Cherednichenko, Sergey V. Egazar’yants, Alexey V. Khoroshilov and Pavel I. Ivanov10.1016/j.mencom.2023.10.031Materials Today Catalysis
Volume 3, November 2023, 100028
Isobutanol
HMFI/SiC composite
catalysis
arenes
C2-C4 olefins
propylene
green hydrocarbons
2023Highly active and stable copper ferrite supported on beta-SiC foam for decomposition of SO3 in the Sulfur-Iodine cycle for H2 productionSachin Tomar, Sreedevi Upadhyayula10.1016/j.ijhydene.2022.12.062Powder Technology Volume 427, 1 September 2023, 118749beta-SiC foam
S-I cycle
SO3 reduction
Pressure drop
Catalytic performances
Hydrogen production
H2
2024Influence of synthesis conditions of Co/SiC and TiC-SiC catalyst on H2 production from NH3M. Pinzon, A.R. de la Osa, A. Romero, A. de Lucas-Consuegra, M.P. Caballero, P. Sanchez10.1016/j.cattod.2023.114418International Journal of Hydrogen Energy Volume 48, Issue 41, 12 May 2023, Pages 15421-15432Ammonia decomposition
Hydrogen production
Cobalt
SiC
TiCSiC
Carbides
2023Methane pyrolysis over porous particlesT. Kreuger, W.P.M. van Swaaij, S.R.A. Kersten10.1016/j.cattod.2023.114058Catalysis today Volumes 413–415, 15 March 2023Thermal decomposition
Methane
Pyrolysis
Hydrogen
Syngas
Kinetics
2023Magnetic induction assisted pyrolysis of plastic waste to liquid hydrocarbons on carbon catalystCuong Duong-Viet, Lai Truong-Phuoc, Lam Nguyen-Dinh, Christophe Michon, Jean-Mario Nhut, Charlotte Pham, Housseinou Ba, Cuong Pham-Huu10.1016/j.mtcata.2023.100028Catalysis Today, 2022, 390–391, 34-47Waste plastic recycling
Carbon catalyst
Induction heating
Pyrolysis
Hydrocarbon production
Carbon-based catalyst can effectively crack model waste plastic based on polyolefins under contactless induction heating and yield gaseous and liquid hydrocarbons fractions at mild reaction temperatures. High catalytic performances are reached thanks to the stable catalyst bed temperature arising from the high heating rate of the induction setup. By comparison to indirect Joule heating which required much higher temperatures, contactless direct induction heating allows a compensation of the internal temperature loss during such highly endothermic process through direct heat targeting. The single carbon-based catalyst combined a high and stable activity with an extremely high stability as a function of cycling tests with pure or mixed polymers. By comparison to the acid or metal based catalysts used in plastic cracking, such low cost carbon catalyst avoids deactivation within cycling tests and therefore provides an efficient and cost-effective route for waste plastic recycling and also as chemical storage means for renewable energy.
2023Hydrodynamic study of the operating window of a stator-rotor vortex chamber reactorXiaojun Lang , Yi Ouyang , Subhajit Dutta , Siyuan Chen , Lingfeng Li , Geraldine Heynderickx ,
Kevin M. Van Geem
10.1016/j.powtec.2023.118749Journal of Environmental Chemical Engineering, 2022, 10 (4), 108195Gas-solid vortex reactor
Operating window
Axial uniformity
Terminal velocity
The gas-solid vortex reactor is promising for process intensification while the huge gas consumption and relatively low solids loading can be a hurdle for some industrial applications. Therefore, an improved design, the stator-rotor vortex chamber (STARVOC) has been proposed. To construct the operating window, five materials with sizes of 300–1000 μm and densities of 700–2330 kg/m3 are tested at varying rotational speeds from 300 to 600 RPM and superficial gas flow rates from 0 to 2.3 m/s. A quantitative assessment of the bed's axial uniformity is conducted and a minimum rotational speed is determined. A semi-empirical correlation is developed for the terminal velocity of particles, enabling obtaining maximum solids loading and identifying maximum rotational speed. It is found that the operating window can be divided into six zones and the appropriate zone for uniform fluidization is identified. This framework provides operational guidelines for STARVOC implementation in drying and reactive applications.
2023Microwave-enhanced methane cracking for clean hydrogen production in shale rocksKeju Yan, Xiangyu Jie, Xiaoqiang Li, Juske Horita, Jacob Stephens, Jianli Hu, Qingwang Yuan10.1016/j.ijhydene.2023.01.052CATALYSIS REVIEWS, 2022, A-O-P, 1-64In-situ hydrogen production
Shale gas reservoirs
Methane cracking
Microwave heating
Catalysts
Steam methane reforming (SMR) generates about 95% of hydrogen (H2) in the U.S. using natural gas as a main feedstock. However, this technology also generates a large amount of carbon dioxide (CO2), a major greenhouse gas causing global warming. Carbon capture and storage (CCS) technique is required, but the cost and safety of storing CO2 underground are a concern. Here we propose a new approach using microwave/electromagnetic irradiation to produce clean hydrogen from unrecovered hydrocarbons within petroleum reservoirs. Solid carbon or CO2 produced during this process will be simultaneously sequestrated underground without involving CCS. In this paper, we perform a series of experiments to investigate the in-situ hydrogen production from shale gas (methane) conversion by passing a methane stream through a packed shale rock sample heated by microwave. We found that methane conversion was significantly enhanced in the presence of Fe and Fe3O4 particles as catalysts, with a conversion of 40.5% and 100% at reaction temperature of 500 °C and 600 °C, respectively. Methane conversion is promoted at a lower reaction temperature by the catalytic effect of minerals in shale. Additionally, the influences of catalysts, shale rock, and methane flow rate are characterized.
2023Solar hydrogen production from ethanol-water vapours over metal/TiO2 photocatalysts supported on β-SiC alveolar foamsPatricia García-Munoz, Javier Ivanez, Víctor A. de la Pena O’Shea, Nicolas Keller, Fernando Fresno10.1016/j.cattod.2022.12.018Applied Catalysis B: Environmental, 2021, 297, 120450Photocatalysis
Hydrogen
Alveolar β-SiC foam
Solar reactor
Solar fuels
In this work, we have explored the feasibility of alveolar open-cell β-SiC foams as catalyst support for solar hydrogen production. For that purpose, Pt and Ru nanoparticles have been obtained, by means of photoassisted synthesis, on TiO2-coated foams and tested in gas-phase hydrogen production from water-ethanol mixtures in a tubular reactor coupled to a compound parabolic solar collector (CPC). Subnanometre-sized metal or metal/oxide nanoparticles are obtained for Pt/TiO2/SiC and Ru/TiO2/SiC foams, respectively, where co-catalyst nanoparticles decorate the TiO2 coating which in turn is attached to the SiC foam through an amorphous SiO2 washcoat formed by SiC pre-calcination. In solar photocatalytic reactions, all of the assayed foam-supported photocatalysts are active for the production of hydrogen, with Pt/TiO2 ones being the most active and foam pore size exerting little influence on hydrogen outcome. In the best conditions, 14 % UV-to-hydrogen (equivalent to 0.49 % solar-to-hydrogen) conversion efficiency, with photonic efficiency higher than 30 %, is attained.
2022COx-free hydrogen production from ammonia at low temperature using Co/SiC catalyst: Effect of promoterM. Pinzón, A. Romero, A. de Lucas-Consuegra, A.R. de la Osa, P. Sánchez10.1016/j.cattod.2021.12.005ACS Catal., 2021, 11, 13423–13433Ammonia decomposition, hydrogen production, Co, Cobalt, SiC support, promoters
2021Support and gas environment effects on the preferential oxidation of carbon monoxide over Co3O4 catalysts studied in situThulani M. Nyathi, Mohamed I. Fadlalla, Nico Fischer, Andrew P.E. York, Ezra J. Olivier, Emma K. Gibson, Peter P. Wells, Michael Claey10.1016/j.apcatb.2021.120450Microchemical Journal, 2021, 169, 106574Co-PrOx, Co3O4, Support effects, Gas environment effects, In situ characterisation
2022Photocatalytic degradation of polystyrene nanoplastics in water. A methodological studyPatricia García-Muñoz, Paul Henri Allé, Calogera Bertoloni, Alvaro Torres, María Ulagares de la Orden, Joaquín Martínez Urreaga, Marie-Antoinette Dziurla, Fernando Fresno, Didier Robert, Nicolas Keller10.1016/j.jece.2022.108195Journal of Catalysis, 2021, 395, 70–79Nanoplastics, TiO2 photocatalysis, Characterization tools, Total organic carbon, Methodology, Water treatment
2022Silicon carbide in catalysis: from inert bed filler to catalytic support and multifunctional materialShekhar R Kulkarni, Vijay K. Velisoju, Fernanda Tavares, Alla Dikhtiarenko, Jorge Gascon, and Pedro Castaño10.1080/01614940.2022.2025670Materials Letters, 2021, 290, 129497SiC, silicon carbide
2021GaPt Supported Catalytically Active Liquid Metal Solution Catalysis for Propane Dehydrogenation–Support Influence and Coking StudiesNarayanan Raman, Moritz Wolf, Martina Heller, Nina Heene-Würl, Nicola Taccardi, Marco Haumann, Peter Felfer, and Peter Wasserscheid10.1021/acscatal.1c01924Applied Catalysis B: Environmental, 2021, 284, 119613Supported liquid catalysis, SCALMS, Ga, gallium, Pt, platinum, DH, dehydrogenation, coking
2013Modulation of the textures and chemical nature of C–SiC as the support of Pd for liquid phase hydrogenationXingyun Li, Xiulian Pan, Yonghua Zhou, Xinhe Bao10.1016/j.carbon.2013.01.013Chem. Rev., 2021, 121 (17), 10559–10665surface tailoring of SiC, Pd, hydrogenation, PTA
2019Tailoring the Surface Structure of Silicon Carbide Support for Copper Catalyzed Ethanol DehydrogenationMeng-Yue Li,Wen-Duo Lu, Lei He, Ferdi Schüth and An-Hui Lu10.1002/cctc.2018017Applied Catalysis B: Environmental, 2021, 286, 119904surface tailoring of SiC, Ethanol dehydrogenation SiC, silicon carbide, Cu, copper
1986THE PREPARATION AND USE OF HIGH SURFACE AREA SILICON CARBIDE CATALYST SUPPORTSAlbert Vannice, Yu-Lin Chao and Robert Mark Friedman10.1016/0166-9834(86)80008-2Journal of Industrial and Engineering Chemistry, 2021, 94, 326–335
2009Chemical Properties of Oxidized Silicon Carbide Surfaces upon Etching in Hydrofluoric AcidSarit Dhar, Oliver Seitz, Mathew D Halls, Sungho Choi, Yves J Chabal, Leonard C Feldman10.1021/ja9053465International Journal of Hydrogen Energy30 June 2020silicon carbide, SiC, surface etching, HF, Hydrofluoric acid
2019Highly effective microwave catalytic direct decomposition of H2S over carbon encapsulated Mo2C–Co2C/SiC compositeJianan Chen, Wentao Xu, Jun Zhu, Xianyou Wang, Jicheng Zhou10.1016/j.ijhydene.2019.08.054Journal of the European Ceramic Society, 2020, 40 (5), 1869-1876Direct H2S decomposition, Microwave selective catalytic effect, Microwave catalysis, Mo2C–Co2C/SiC@C microwave catalyst, H2 generation
2020Characterization of SiC ceramics with complex porosity by capillary infiltration: Part B - Filling by molten silicon at 1500 °CJ. Roger, M. Avenel, L. Lapuyade10.1016/j.jeurceramsoc.2019.12.050Catalysis Today, 2020, 343, 176-182SiC, Molten silicon, Microstructure evolution, Infiltration kinetic, Washburn equation
2021A versatile method for the quantification of 100 SVOCs from various families: Application to indoor air, dust and bioaccessibility evaluationAlexandre Sonnette, Olivier Delhomme, Laurent Y. Alleman, Patrice Coddeville, Maurice Millet10.1016/j.microc.2021.106574Journal of the European Ceramic Society, 2020, 40, 1859-1868Thermal-desorption, SPME, Indoor air, Dust, Bioaccessibility, Derivatization
2020Surface modification of Co3O4 nanocubes with TEOS for an improved performance in the Fischer-Tropsch synthesisLebohang Macheli, Amitava Roy, Emanuela Carleschi, Bryan P Doyle, Eric van Steen10.1016/j.cattod.2018.10.018Applied Catalysis A: General, 2020, 608, 117866Cobalt, Metal-support interaction (MSI), Silica, Fischer-Tropsch
2020Characterization of SiC ceramics with complex porosity by capillary infiltration: Part A - Filling by hexadecane at 20 °CJ. Roger, M. Avenel, L. Lapuyade10.1016/j.jeurceramsoc.2019.12.049Applied Catalysis A: General, 2020, 601, 117619SiC, Pore characterization, Infiltration kinetic, Infiltration mechanism, Washburn equation
2021Tuning catalytic performance in Fischer-Tropsch synthesis by metal-support interactionsLebohang Macheli, Emanuela Carleschi, Bryan P. Doyle, Gerard Leteba, Eric van Steen10.1016/j.jcat.2020.12.023Catalysis Today, 2020, 362, 72-80Metal-support interactions, Cobalt, Silica, Fischer-Tropsch
2021A new method for synthesis of a HMFI/SiC compositeAlexey G. Dedov, Alexander A. Karavaev, Alexey S. Loktev, Alexey S. Mitinenko, Kirill A. Cherednichenko, Ilya I. Moiseev10.1016/j.matlet.2021.129497Chemical Engineering Journal, 2020, 393, 124746HMFI/SiC composite, Hydrothermal-microwave synthesis, Porous materials, Zeolites
2020Synthesis and catalytic performance of zeolite-Y supported on silicon
carbide in n-heptane cracking
Aasif A. Dabbawala, Balasubramanian V. Vaithilingam, Hemant Mittal, Yasser Al Wahedi, Shaihroz Khan, Tony Joseph, Gnana Singaravel, Stephane Morin, Mikael Berthod, Saeed M. Alhassan10.1016/j.apcata.2020.117866Atmospheric Pollution Research, 2020, 11, 1217-1225Zeolite-Y, SiC, Supported catalyst, n-heptane, Cracking
2021Insights into enhanced stability and activity of silica modified SiC supported iron oxide catalyst in sulfuric acid decompositionShailesh Pathak, Shikha Saini, Kishore Kondamudi, Sreedevi Upadhyayula, Saswata Bhattacharya10.1016/j.apcatb.2020.119613Environmental Technology & Innovation, 2020, 20, 101094Metal- support interaction, Endothermic reaction, SiC supported iron catalyst, Iodine-Sulfur (I-S) process
2020Screening of catalysts for the oxidative dehydrogenation of ethyl lactate to
ethyl pyruvate, and optimization of the best catalysts
M. Huchede, D. Morvan, V. Bellière-Baca, J.M.M. Millet10.1016/j.apcata.2020.117619Catalysis Science & Technology, 2020, 10, 5487-5500Ethyl lactate, Ethyl pyruvate, Oxidative dehydrogenation, Molecular oxygen, Screening of catalysts, Polyoxometalate catalysts
2019Synthesis and characterization of Pt on novel catalyst supports for the H2 production in the Westinghouse cycleJusto Lobato, Sergio Dı´az-Abad, M Carmen Pelaez, Marıa Millan, Manuel A. Rodrigo10.1016/j.ijhydene.2019.10.154Journal of Catalysis, 2020, 383, 297–303Catalyst support, Durability, SiC/TiC, SO2 electro-oxidation, Westinghouse cycle
2019Efficient hydrogen production from partial oxidation of propane over SiC doped Ni/Al2O3 catalystMingzheng Liao, Chao Wang, Enqi Bu, Ying Chen, Zhengdong Cheng, Xianglong Luo, Riyang Shu, Juhui Wu10.1016/j.egypro.2019.01.419Journal of the European Ceramic Society, 2020, 40, 1859-1868Hydrogen production, propane partial oxidation, Ni/Al2O3, SiC
2021Porous Silicon Carbide (SiC): A Chance for Improving Catalysts or Just Another Active-Phase Carrier?Giulia Tuci, Yuefeng Liu, Andrea Rossin, Xiangyun Guo, Charlotte Pham, Giuliano Giambastiani, and Cuong Pham-Huu10.1021/acs.chemrev.1c00269RSC Adv., 2020, 10, 3817-3825SiC, silicon carbide
1997High surface area silicon carbide as catalyst support characterization and stabilityR. Moene, M. Makkee, J.A. Moulijn10.1016/S0926-860X(97)00326-8Catalysis Today, 2020, 343, 176-182High surface area silicon carbide, Catalyst support, Stability, Oxidation, Chemical vapour deposition
2021SiO2/SiC supports with tailored thermal conductivity to reveal the effect of surface temperature on Ru-catalyzed CO2 methanationElspeth M. Petersen, Radhika G. Rao, Brandon C. Vance, Jean-Philippe Tessonnier10.1016/j.apcatb.2021.119904ChemCatChem, 2019, 11, 481–4CO2 methanation, SiC, silicon carbide, surface oxidation, Ni, nickel, thermal conductivity
2021Hydrogen production by ammonia decomposition over ruthenium supported on SiC catalystM. Pinzón, A. Romero, A. de Lucas Consuegra, A.R. de la Osa, P. Sánchez10.1016/j.jiec.2020.11.003International Journal of Hydrogen Energy, 2019, 44 (47), 25680-25694ammonia decomposition, hydrogen production, Ru, ruthenium catalyst, SiC support
2013A comparison of Ni/SiC and Ni/Al2O3 catalyzed total methanation for production of synthetic natural gasGuoquan Zhang, Tianjun Sun, Jiaxi Peng, Sheng Wang, Shudong Wang10.1016/j.apcata.2013.04.037International Journal of Hydrogen Energy, 2019, 45, 25672-25680Methanation, SiC Stability, Carbon deposition, Regeneration
2020Syngas production via microwave-assisted dry reforming of methaneIgnacio de Dios García, Andrzej Stankiewicz, Hakan Nigar10.1016/j.cattod.2020.04.045Chemical Engineering Journal, 2019, 362, 53-62Heterogeneous catalysis, Microwave heating, Dry reforming, Syngas, Methane, Carbon dioxide
2020Microwave-activated structured reactors to maximize propylene selectivity in the oxidative dehydrogenation of propaneAdrian Ramirez, Jose L.Hueso, Reyes Mallada, Jesus Santamaria10.1016/j.cej.2020.124746Chemical Engineering Journal, 2019, 362, 53-62Microwave chemistry, Propylene production, Silicon carbide, Oxidative dehydrogenation, Structured reactors
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2016Microtomography-based numerical simulations of heat transfer and fluid flow through β-SiC open-cell foams for catalysisXiaolei Fan, Xiaoxia Ou, Fei Xing, Glen A. Turley, Petr Denissenko, Mark A. Williams, Nelly Batail, Charlotte Pham, Alexei A. Lapkin10.1016/j.cattod.2015.12.012Chemical Engineering Journal, 2013, 221, 44–54Foam, finite element analysis, FEA, Effective thermal conductivity, Computational fluid dynamics (CFD), fluid flow
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2013β-SiC foams as a promising structured photocatalytic support for water and air detoxificationN. Kouamé, R. Masson, D. Robert, N. Keller, V. Keller,10.1016/j.cattod.2012.12.008Chemical Engineering Journal, 2013, 222, 265–273Foam, photocatalyst, water treatment, air treatment, TiO2, diuron, methylethylketone
2014N-doped carbon nanotubes decorated SiC as a metal-free catalyst for partial oxidation of H2SCuong Duong-Viet, Lai Truong-Phuoc, Tung Tran-Thanh, Jean-Mario Nhut, Lam Nguyen-Dinh, Izabela Janowska, Dominique Begin, Cuong Pham-Huu10.1016/j.apcata.2014.06.010ACS Catalysis, 2013, 3, 393−404H2S, hydrogen sulfide, selective oxidation, nitrogen-doped carbon nanotubes, meral-free catalyst
2014N-doped carbon nanotubes on SiC as metal-free catalystCuong Duong-Viet, Housseinou Ba, Yuefeng Liu, Lai Truong-Phuoc, Jean-Mario Nhut, Cuong Pham-Huu10.1016/S1872-2067(14)60116-9Catalysis Today, 2012, 189, 101-110H2S, hydrogen sulfide, selective oxidation, dehydrogenation, ethylbenzene, nitrogen-doped carbon nanotubes, metal-free catalyst
2015Preparation of Ni–Mg/-SiC catalysts for the methane tri-reforming: Effect of the order of metal impregnationJesús Manuel García-Vargas, José Luís Valverde, Javier Díez, Paula Sánchez, Fernando Dorado10.1016/j.apcatb.2014.09.044Chemical Engineering Journal, 2012, 185-186, 294-299Methane, reforming, tri-reforming, Ni, nickel
2013Characteristics and CLOU performances of a novel SiO2-supported oxygen carrier prepared from CuO and β-SiC.S.B. Peterson, G. Konya, C.K. Clayton, R.J. Lewis, B.R. Wilde, E.M. Eyring, K.J. Whitty10.1021/ef401365hIndustrial and Engineering Chemistry Research, 2012, 51, 15011-15017CLC, CLOU, chemical looping combustion, oxygen carrier, Cu, CuO, copper, SiO2, SiC, stability, attrition
1999Influence of the preparation conditions on the synthesis of high surface area SiC for use as a heterogeneous catalyst supportN. Keller, C. Pham-Huu, S. Roy, M.J. Ledoux, C. Estournes, J. Guille10.1023/A:1004681806843Journal of Chemical Technology and Biotechnology, 2012, 87, 360-367SiC synthesis, operation conditions
2005New catalysts based on silicon carbide support for improvements in the sulfur recovery. New silicon carbide nanotubes as catalyst support for the trickle-bed H2S oxidationN. Keller, R. Vieira, J.M. Nhut, C. Pham-Huu, M.J. Ledoux10.1590/S0103-50532005000400003Applied Catalysis A: General, 2012, 433–434, 41–48H2S, hydrogen sulfide, selective oxidation, trickle-bed, SiC nanotubes, Ni, nickel, NiS2 ,nickel sulfide, confinement effect
2005New catalysts based on silicon carbide support for improvements in the sulfur recovery. Silicon carbide as support for the selective H2S oxidation.N. Keller, R. Vieira, J.M. Nhut, C. Pham-Huu, M.J. Ledoux10.1590/S0103-50532005000400003Master’s thesis manuscript, NTNU, under the direction of A. Holmen, submitted June 2012H2S, hydrogen sulfide, selective oxidation, Ni, nickel, NiS2 ,nickel sulfide, Fe, iron, Fe2O3, iron oxide, hydrophilic, hydrophobic, hydrophilicity, hydrophobicity
1997High temperature removal of H2S over iron oxide supported SiC sorbentC. Pham-Huu, C. Estournes, B. Heinrich, C. Crouzet, M.J. Ledoux10.1051/jp4:19971277Applied Catalysis A: General, 2012, 431– 432, 49– 56H2S, hydrogen sulfide, selective oxidation, Fe, iron, Fe2O3, iron oxide, stability
2005High surface area submicrometer-sized beta-SiC particles grown by shape memory synthesis methodN. Keller, O. Reiff, V. Keller, M.J. Ledoux10.1016/j.diamond.2005.01.026Applied Catalysis A: General, 2012, 419–420, 31–40SiC synthesis, SiC manufacture, carbon nanodiamond
2001Silicon carbide a novel catalyst support for heterogeneous catalysisLedoux, M.J., Pham-Huu, C.10.1023/A:1014092930183Environ Sci Pollut Res, 2012, 19, 3727–3734H2S, selective oxidation, Ni, nickel, nickel sulfide, Fe, iron, iron oxide, hydrophilic, hydrophobic, hydrophilicity, hydrophobicity, n-butane, maleic acid, maleic anhydride, auomotive exhaust, three-way catalyst, TWC, dopant, Ce, nanotubes
2014Fischer-Tropsch reaction on a thermally conductive and reusable silicon carbide supportLiu, Y., Ersen, O., Meny, C., Luck, F., Pham-Huu, C.10.1002/cssc.201300921Catalysis Today, 2012, 187, 173–182Fischer-Tropsch, FTS, thermal conductivity, review, TiO2, titania, titanium dioxide, dopant, Ru, Ca, Al2O3, TEM, EFTEM, XPS, tomography, support recycling, support recovery
2007ZSM-5 coatings on β-SiC monoliths: possible new structured catalyst for the methanol to olefins processS. Ivanova, B. Louis, B. Madani, J.P. Tessonnier, M.J. Ledoux, C. Pham-Huu10.1021/jp067535kScience, 2012, 335, 835-838ZSM-5, zeolite, MTO, methanol to olefins, open-cell foam, stability
1999Preparation and characterization of SiC microtubesN. Keller, C. Pham-Huu, M.J. Ledoux, C. Estournes, G. Ehret10.1016/S0926-860X(99)00223-9Fuel, 2012, 95, 587–598microtubes, SiOxCy, oxicarbide, amorphous layer, soda treatment
2004Pd/SiC exhaust gas catalyst for heavy-duty engines: improvement of catalytic performances by controlling the location of the active phase on the supportJ.M. Nhut, L. Pesant, N. Keller, C. Pham-Huu, M.J. Ledoux10.1023/B:TOCA.0000029774.03973.a6Advanced Engineering Materials, 2011, 13(3), 122-127Pd, palladium, exhaust gas catalyst, total oxidation of methane, hydrophobic, hydrophilic, hydrophobicity, hydrophilicity, active phase location
2014Heat transfer study with and without Fischer-Tropsch reaction in a fixed bed reactor with TiO2, SiO2, and SiC supported cobalt catalystsX. Zhu, X. Lu, X. Liu, D. Hildebrandt, D. Glasser10.1016/j.cej.2014.02.089Industrial and Engineering Chemistry Research, 2011, 50, 4329-4334Fischer-tropsch Synthesis, FTS, Fixed bed reactor, heat transfer, effective thermal conductivity coefficient, Co, cobalt
2012Residence time distribution, axial liquid dispersion and dynamic-static liquid mass transfer in trickle flow reactor containing β-SiC open-cell foamsSaber M., Huu T.T., Pham-Huu C., Edouard D.10.1016/j.cej.2012.01.045Applied Catalysis A: General, 2011, 409–410, 113–121open-cell foam, trickle bed reactor, axial dispersion, mass transfer
2012Axial dispersion based on the residence time distribution curves in a millireactor filled with β-sic foam catalystSaber M., Pham-Huu C., Edouard D.10.1021/ie3017829Catalysis Today, 2011, 161, 3–7open-cell foam, axial dispersion, mass transfer, milli-reactor
2011Radial dispersion in liquid upflow through solid SiC foamsTruong Huu T., Philippe R., Nguyen P., Edouard D., Schweich, D.10.1021/ie1017942Applied catalysis A: General, 2011, 397, 62-72open-cell foam, radial dispersion, mass transfer
2012Performances of SiC foams as support for Pd based methane combustion catalystP. Marin, S. Ordonez, F.V. Diez10.1002/jctb.2726Catalysis Today, 2011, 176, 298–302open-cell foam, kinetic modeling, catalytic combustion, methane combustion, low temperature burners, Pd, palladium, stability
2011Methanol dehydration to dimethyl ether in a platelet milli-reactor filled with H-ZSM5/SiC foam catalystYu Liu, Seetharamulu Podila, Dinh Lam Nguyen, David Edouard, Patrick Nguyen,Charlotte Pham, Marc Jacques Ledoux, Cuong Pham-Huu10.1016/j.apcata.2011.09.035Applied Catalysis A: General, 2011, 391, 443–454methanol dehydration, dimethyl ether, milli-reactor, open cell foam, zeolite, ZSM5, stability
2013Evaluation of the use of ceramic foams as catalyst supports for reverse-flow combustorsClaire R. Thompson, Pablo Marín, Fernando V. Díez, Salvador Ordóñez10.1016/j.cej.2013.01.080Nanoscale, 2010, 2(12), 2668-78open-cell foam, afterburner, lean fuel, dynamic modeling, methane combustion, catalytic combustion, reverse flow reactor, Pd, palladium
2012Catalytic performances of MoVTeNbO catalyst on SiC in ODH of ethylene and ammoxidation of propaneT.T. Nguyen, L. Burel, D.L. Nguyen, C. Pham-Huu, J.M.M. Millet10.1016/j.apcata.2012.04.038International Journal of Heat and Mass Transfer, 2010, 53, 3807–3816oxides catalyst, open-cell foam, oxidative dehydrogenation of ethane, ammoxidation of propane, ODH, dip coating, stability
2014Silicon carbide foam decorated with carbon nanofibers as catalytic stirrer in liquid-phase hydrogenation reactionsLai Truong-Phuoc, Tri Truong-Huu, Lam Nguyen-Dinh, Walid Baaziz, Thierry Romero, D. Edouard, D. Begin, I. Janowska, C. Pham-Huu10.1016/j.apcata.2013.09.032Applied Catalysis A: General, 2010, 385, 52–61open-cell foam, carbon nanofibers, CNF, liquid phase hydrogenation, Pd, palladium, catalytic stirrer, stability
2014Beta-silicon carbide as a catalyst support in the FT synthesis: influence of the modification of the support by a pore agent and acidic treatmentJ.A. Diaz, M. Calvo-Serrano, A. Raquel de la Osa, A.M. Garcia-Minguillan, A. Romero, A. Giroir-Fendler, J.L. Valverde10.1016/j.apcata.2014.01.021Catalysis Today, 2010, 150, 133–139Fischer-tropsch Synthesis, FTS, acid treatment, pore agent, macropores, pore size distribution, impurities, Co, cobalt
2008Cu-Y zeolite supported on silicon carbide for the vapour phase oxidative carbonylation of methanol to dimethyl carbonateG. Rebmann, V. Keller, M.J. Ledoux, N. Keller,10.1039/b712705gJournal of American Chemical Society., 2009, 131 (46), 16808-13oxidative carbonylation of methanol, dimethyl carbonate, zeolite, Y, stability
2013Fischer-Tropsch Synthesis on SiC-supported Cobalt CatalystsA. Lillebo, S. Havik, E.A. Blekkan, A. Holmen10.1007/s11244-013-0032-3Applied Catalysis A: General, 2009, 360, 154–162Fischer-tropsch Synthesis, FTS, biomass, impurities, Co, cobalt
2002Beta zeolite supported on a macroscopic pre-shaped SiC as a high performance catalyst for liquid-phase benzoylationG. Winé, J.P. Tessonnier, C. Pham-Huu, M.J. Ledoux10.1039/b206805mJournal of Physical Chemistry C, 2009, 113, 17711-17719zeolite, beta, liquid-phase benzoylation
1997Molybdenum oxycarbide hydrocarbon isomerization catalysts: cleaner fuels for the futureAndrew P.E. York, Cuong Pham-Huu, Pascal Del Gallo, Marc J. Ledoux10.1016/S0920-5861(96)00134-4Applied Catalysis A: General, 2009, 360, 154-162molybdenum oxycarbide, isomérization, n-heptane, n-octane, sulfur and nitrogen resistance, stability
2004Synthesis and characterization of a new medium surface area TiO2-β-SiC material for use as photocatalystNicolas Keller, Valérie Keller, Elodie Barraud, François Garin, Marc J. Ledoux10.1039/B400993BChemical Engineering Science, 2009, 64, 2607-2616TiO2, titanium dioxide, TiO2-SiC composite, photocatalysis, photocatalyst
20081D SiC decoration of SiC macroscopic shapes for filtration devicesEstelle Vanhaecke, Svetlana Ivanova, Adrien Deneuve, Ovidiu Ersen, David Edouard, Gauthier Winé, Patricl Nguyen, Charlotte Pham, Cuong Pham-Huu10.1039/B806785FCatalysis Today, 2009, 147, S305-S312open-cell foam, SiC nanofibers, filtration, DPF, Diesel particle filter
2008Experimental measurements and multiphase flow models in solid SiC foam bedsDavid Edouard, Maxime Lacroix, Charlotte Pham, Mamadou Mbodji, Cuong Pham-Huu10.1002/aic.11594Chemical Engineering Science, 2009, 64, 5131-5142open-cell foam, flow model, hydrodynamic, trickle-bed, pressure drop, liquid hold-up
2012SiC supported Co catalysts for the Fischer Tropsch SynthesisSindre HavikN/AJournal of Catalysis, 2009, 265, 1-7Fischer-tropsch Synthesis, FTS, acid treatment, pore agent, macropores, pore size distribution, impurities, Co, cobalt
2013High performance structured platelet milli-reactor filled with supported cobalt open cell SiC foam catalyst for the Fischer-Tropsch synthesisYu Liu, David Edouard, Lâm D. Nguyen, Dominique Begin, Patrick Nguyen, Charlotte Pham, Cuong Pham-Huu10.1016/j.cej.2013.02.066Catalysis Communications, 2009, 10, 477-480Fischer-tropsch synthesis, FTS, milli-reactor, open-cell foam, liquid hold-up, Co, cobalt
2013Titania -Decorated Silicon Carbide-Containing Cobalt Catalyst for Fischer−Tropsch SynthesisYuefeng Liu, Benoit de Tymowski, Fabrice Vigneron, Ileana Florea, Ovidiu Ersen, Christian Meny, Patrick Nguyen, Charlotte Pham, Francis Luck, Cuong Pham-Huu10.1021/cs300729pApplied Catalysis A: General, 2009, 359, 151-157TiO2, titanium dioxide, Titania, TiO2-SiC, Fischer-Tropsch synthesis, FTS, EFTEM, NMR, Co particle size, metal-support interaction, Co, cobalt
2012Precursor influence and catalytic behaviour of Ni/CeO2 and Ni/SiC catalysts for the tri-reforming processJesús Manuel García-Vargas, José Luís Valverde, Antonio de Lucas-Consuegra, Beatriz Gómez-Monedero, Paula Sánchez, Fernando Dorado10.1016/j.apcata.2012.04.016Catalysis Today, 2009, 141, 393-396Methane, tri-reforming, TPR, TPD, Ni, nickel, water-gas shift, WGS, stability, methane reforming
2012Co–Ru/SiC impregnated with ethanol as an effective catalyst for the Fischer–Tropsch synthesisBenoit de Tymowski, Yuefeng Liu, Christian Meny, Christophe Lefèvre, Dominique Begin, Patrick Nguyen, Charlotte Pham, David Edouard, Francis Luck, Cuong Pham-Huu10.1016/j.apcata.2012.01.004Catalysis Today, 2009, 141, 397-402Fischer-Tropsch synthesis, FTS, NMR, Co, cobalt, Ru, ruthenium, stability
2012TiO2/SiC Foam-Structured Photoreactor for continuous waste water treatmentNathalie Amoin Kouamé, Didier Roberta, Valérie Keller, Nicolas Keller, Charlotte Pham, Patrick Nguyen10.1007/s11356-011-0719-6Catalysis Today, 2009, 141, 403-408Water treatment, photocatalysis, photocatalyst, photoreactor, TiO2, titania, titanium dioxide, TiO2-SiC, open-cell foam, Diuron
2012FTS fuels production over different Co/SiC catalystsR. de la Osa, A. De Lucas, J. Díaz-Maroto, A. Romero, J.L. Valverde, P. Sánchez.10.1016/j.cattod.2011.12.029Journal of Nanoscience and Nanotechnology, 2008, 8, 1–6Fischer-Tropsch synthesis, FTS, Co, cobalt, promoter, Ca, calcium
2012Supported Iron Nanoparticles as Catalysts for Sustainable Production of Lower OlefinsHirsa M. Torres Galvis, Johannes H. Bitter, Chaitanya B. Khare, Matthijs Ruitenbeek, A. Iulian Dugulan, and Krijn P. de Jong10.1126/science.1215614ChemSusChem, 2008, 1, 851-857Fischer-Tropsch, FTS, Fe, Fe2O3, iron, iron oxide, lower olefins, promoter, S, sulfur, Ca, calcium
2012Performing the best composition of supported Co/SiCcatalyst for selective FTS diesel productionAna Raquel de la Osa, Antonio de Lucas, Luz Sánchez-Silva, Javier Díaz-Maroto, José Luis Valverde, Paula Sánchez10.1016/j.fuel.2011.11.002Green Chemistry, 2008, 10, 207-213Fischer-Tropsch synthesis, FTS, Co, cobalt, diesel production, promoter, Ca, calcium
2011Preliminary study of the use of β-SiC foam as a photocatalytic support for water treatmentN.A. Kouamé, D. Roberta, V. Keller, N. Keller, C. Pham, P. Nguyen10.1016/j.cattod.2010.10.045Journal of Materials Chemistry, 2008, 18, 4654-4662water treatment, photocatalysis, photocatalyst, photoreactor, TiO2, titania, titanium dioxide, TiO2-SiC, open-cell foam, Diuron
2011Silicon Carbide Foam Composite Containing Cobalt as a Highly Selective and Re-Usable Fischer-Tropsch Synthesis CatalystLacroix Maxime, Dreibine Lamia, De Tymowski Benoit, Vigneron Fabrice, Edouard David, Begin Dominique, Nguyen Patrick, Pham Charlotte, Savin-Poncet Sabine, Luck Francis, Ledoux Marc-Jacques, Pham-Huu Cuong10.1016/j.apcata.2011.02.012AIChE Journal, 2008, 54, 2823–2832Fischer-Tropsch synthesis, FTS, open-cell foam, Co, cobalt, alumina coating, Al2O3 coating
2011Influence of the catalytic support on the industrial Fischer–Tropsch synthetic diesel productionA.R. de la Osa, A. De Lucas, A. Romero, J.L. Valverde, P. Sánchez10.1016/j.cattod.2010.12.010Diamond and Related Materials, 2008, 17, 1867-1870Fischer-tropsch synthesis, FTS, Co, cobalt, diesel production
2011Innovative porous SiC-based materials: from nanoscopic understandings to tunable carriers serving catalytic needsPatrick Nguyen, Charlotte Pham10.1016/j.apcata.2010.07.054Chemical Engineering Journal, 2008, 144, 299-311Tailored porosity, tailored surface chemistry thermal conductivity, photocatalysis, photocatalyst, H2S oxidation, Fischer-Tropsch synthesis
2010Catalytic growth of silicon carbide composite with nanoscopic properties and enhanced oxidative resistance as catalyst supportAdrien Deneuve, Ileana Florea, Ovidiu Ersen, Patrick Nguyen, Charlotte Pham, Dominique Begin, David Edouard, Marc-Jacques Ledoux, Cuong Pham-Huu10.1016/j.apcata.2010.06.043Studies in Surface Science and Catalysis, 2008, 174, 1307-1310Composite, SiC nanofibers, oxidative resistance
2009Selective Deposition of Palladium Nanoparticles inside the Bimodal Porosity of β-SiC Investigated by Electron TomographyIleana Florea, Matthieu Houlle, Ovidiu Ersen, Lucian Roiban, Adrien Deneuve, Izabela Janowska, Patrick Nguyen, Charlotte Pham, and Cuong Pham-Huu10.1021/jp905968nJournal of American Chemical Society, 2007, 129, 3383-3391Pd, palladium, bimodal porosity, Electron tomography, ET, liquid phase hydrogenation, hydrogenation of cinnamaldehyde
2007SiC as stable high thermal conductive catalyst for enhanced SR processF.Basile, P. Del Gallo, G. Fornasaria, D. Gary, V. Rosetti, A. Vaccari10.1016/S0167-2991(07)80150-9Journal of Physical Chemistry C, 2007, 111, 4368-4374Methane reforming, steam methane reforming, SMR, Ni, nickel
2007Suppoted BETA zeolite on preshaped beta-SiC as clean Friedel-Crafts liquid-phase catalystG. Winé, M.J. Ledoux, Cuong Pham-Huu10.1007/s11244-007-0249-0Studies in Surface Science and Catalysis, 2007, 167, 313-318Zeolite, BETA zeolite, Friedel-Crafts, acylation of anisole
2010High surface-to-volume hybrid platelet reactor filled with catalytically grown vertically aligned carbon nanotubesYu Liu, Izabela Janowska, Thierry Romero, David Edouard, Lâm D. Nguyen, Ovidiu Ersen, Valérie Keller, Nicolas Keller, Cuong Pham-Huu10.1016/j.cattod.2009.09.007Topics in Catalysis, 2007, 45, 111-116host structure, VA-CNT, vertically aligned carbon nanotube
2009Deposition and characterisation of TiO2 coatings on various supports for structured (photo)catalytic reactorsPhilippe Rodriguez, Valérie Meille, Stéphanie Pallier, Mohamad Ali Al Sawah10.1016/j.apcata.2009.03.013Journal of Molecular Catalysis A: Chemical, 2007, 278, 64-71Titanium dioxide, TiO2 coating, titania coating, photocatalysis, photocatalyst, dip coating, open-cell foam
2009Hydrodynamic and mass transfer efficiency of ceramic foam packing applied to distillationJulien Lévêque, David Rouzineau, Michel Prévost, Michel Meyer10.1016/j.ces.2009.02.010Applied Catalysis B: Environmental, 2007, 76, 300-310Hydrodynamic, mass transfer, distillation, open-cell foam, packing, catalytic distillation
2009Effect of structure and thermal properties of a Fischer-Tropsch catalyst in a fixed bedRégis Philippe, Maxime Lacroix, Lamia Dreibine, Cuong Pham-Huu, David Edouard, Sabine Savin, Francis Luck, Daniel Schweich10.1016/j.cattod.2009.07.058Chemical Engineering Science, 2007, 62, 3259-3267Fischer-Tropsch synthesis, fixed bed reactor, modeling, Co, cobalt, open-cell foam, pellets, heat transfer
2009Towards a more realistic modeling of solid foam: Use of the pentagonal dodecahedron geometryTri Truong Huu, Maxime Lacroix, Cuong Pham Huu, Daniel Schweich, David Edouard10.1016/j.ces.2009.08.028Catalysis Communications, 2006, 7, 768-772modeling, open-cell foam, pressure drop, mass transfer, surface area
2009Influence of the zeolite synthesis route on its catalytic properties in the methanol to olefin reactionSvetlana Ivanova, Charline Lebrun, Estelle Vanhaecke, Cuong Pham-Huu, Benoit Louis10.1016/j.jcat.2009.03.016Journal of Molecular Catalysis A: Chemical, 2006, 248, 113-120Zeolite, ZSM-5, methanol to olefin, MTO, open-cell foam
2009Microwave heating effects on acylation of anisole, catalyzed by BEA zeolite supported on β-SiCGauthier Winé, Estelle Vanhaecke, Svetlana Ivanova, Raymond Ziessel, Cuong Pham-Huu10.1016/j.catcom.2008.10.014Journal of Brazilian Chemical Society, 2005, 16, 514-519Microwave assisted reaction, acylation of anisole, BEA, zeolite
2009Binderless HZSM-5 coating on β-SiC for different alcohols dehydrationS. Ivanova, E. Vanhaecke, L. Dreibine, B. Louis, Ch. Pham, C. Pham-Huu10.1016/j.apcata.2009.02.024Journal of Brazilian Chemical Society, 2005, 16, B127202-209Zeolite, ZSM-5, alcohols dehydrogenation, open-cell foam, alcohol to olefins
2009Influence of the oxygen pretreatment on the CO2 reforming of methane on Ni/β-SiC catalystDinh Lam Nguyen, Pascaline Leroi, Marc Jacques Ledoux, Cuong Pham-Huu10.1016/j.cattod.2008.10.019Diamond and Related Materials, 2005, 14, 1353-1360Ni, nickel, methane reforming, CO2 reforming
2009Fe2O3/β-SiC: A new high efficient catalyst for the selective oxidation of H2S into elemental sulfurPatrick Nguyen, Jean-Mario Nhut, David Edouard, Charlotte Pham, Marc-Jacques Ledoux, Cuong Pham-Huu10.1016/j.cattod.2008.10.047Topics in Catalysis, 2004, 30-31, 353-358Selective oxidation, H2S oxidation, Fe, Fe2O3, iron, iron oxide, thermal conductivity, heat transfer
2009Pressure drop measurements and hydrodynamic model description of SiC foam composites decorated with SiC nanofiberDavid Edouard, Svetlana Ivanova, Maxime Lacroix, Estelle Vanhaecke, Charlotte Pham, Cuong Pham-Huu10.1016/j.cattod.2008.06.002Journal of Materials Chemistry, 2004, 14, 1887-1895hydrodynamic modeling, open-cell foam, pressure drop, specific surface area, SiC nanofiber
2008Towards the oxygenated phase coverage rate of β-SiC surfaceNicolas Keller, François Di Grégorio, Cuong Pham-Huu, Valérie Keller10.1016/j.diamond.2008.03.034Catalysis Today, 2004, 91-92, 53-58H/D exchange, D2O, surface analysis, amorphous layer, SiOxCy, oxicarbide, soda treatment
2008Pressure drop modeling on SOLID foam: State-of-the art correlationDavid Edouard, Maxime Lacroix, Cuong Pham Huu, Francis Luck10.1016/j.cej.2008.06.007Applied Catalysis A: General, 2004, 266, 21-27Pressure drop open-cell foam, modeling, open-cell foam
2008Benzoylation of anisole catalysed by Ga/SBA-15 supported on β-SiCF.Z.El Berrichi, B. Louis, L. Cherif, M.J. Ledoux, C. Pham. Huu10.1016/S0167-2991(08)80129-2Materials Letters, 2004, 58, 970-974water treatment, photocatalysis, photocatalyst, photoreactor, TiO2, titania, titanium dioxide, TiO2-SiC, open-cell foam, Diuron
2007BETA zeolite supported on silicon carbide for Friedel-Crafts fixed-bed reactionsGauthier Winé, Zora El Berrichi, Cuong Pham-Huu10.1016/j.molcata.2007.08.018Chemical Communications, 2002, , 2418-2419zeolite, BETA zeolite, Friedel-Crafts acylation, benzoylation of anisole, stability
2007High thermal conductive β-SiC for selective oxidation of H2S: A new support for exothermal reactionsP. Nguyen, D. Edouard, J.-M. Nhut, M.J. Ledoux, Ch. Pham, C. Pham-Huu10.1016/j.apcatb.2007.06.007Applied Catalysis A: General, 2002, 234, 191-205selective oxidation, H2S, hydrogen sulfide, Fe, iron, thermal conductivity, heat tranfer, stability, modeling
2007Pressure drop measurements and modeling on SiC foamsMaxime Lacroix, Patrick Nguyen, Daniel Schweich, Cuong Pham-Huu, Sabine Savin-Poncet, David Edouard10.1016/j.ces.2007.03.027CATTECH, 2001, 5, 226-246pressure drop, modeling, open-cell foam, hydrodynamic
2006Acylation of anisole by acetic anhydride catalysed by BETA zeolite supported on pre-shaped silicon carbideGauthier Winé, Cuong Pham-Huu, Marc-Jacques Ledoux10.1016/j.catcom.2006.03.002Journal of Catalysis, 2001, 203, 495-508zeolite, Beta zeolite, Friedel-Crafts, acylation, acetic anhydride, anisole, stability
2006Beta zeolite supported on a β-SiC foam monolith: A diffusionless catalyst for fixed-bed Friedel-Crafts reactionsGauthier Winé, Jean-Philippe Tessonnier, Séverinne Rigolet, Claire Marichal, Marc-Jacques Ledoux, Cuong Pham-Huu10.1016/j.molcata.2005.12.010Applied Catalysis A: General, 2001, 217, 205-217zeolite, Beta zeolite, open-cell foam, Friedel-Crafts, acylation, benzoylation of anisole, stability
2004Ni/SiC: a stable and active catalyst for catalytic partial oxidation of methanePascaline Leroi, Behrang Madani, Cuong Pham-Huu, Marc-Jacques Ledoux, Sabine Savin-Poncet, Jacques Louis Bousquet10.1016/j.cattod.2004.03.009Catalysis Today, 2000, 61, 157-163POX, methane oxidation, Ni, nickel, syngas, stability
2004A high-performance Pt/β-SiC catalyst for catalytic combustion of model carbon particles (CPs)Laurie Pesant, Joseph Matta, François Garin, Marc-Jacques Ledoux, Pierre Bernhardt, Charlotte Pham, Cuong Pham-Huu10.1016/j.apcata.2004.01.033Catalysis Today, 2000, 61, 157-163Pt, platinum, combustion, , stability, soot, DPF, TEM, particle size
2004A new TiO2–β-SiC material for use as photocatalystNicolas Keller, Valérie Keller, François Garin, Marc J. Ledoux10.1016/j.matlet.2003.08.009Journal of Material Science, 1999, 34, 3189-3202photocatalyst, photocatalysis, TiO2, titania, titanium dioxide
2002Low temperature use of SiC-supported NiS2-based catalysts for selective H2S oxidation: Role of SiC surface heterogeneity and nature of the active phaseNicolas Keller, Cuong Pham-Huu, Claude Estournès, Marc J. Ledoux10.1016/S0926-860X(02)00226-0Applied Catalysis A: General, 1999, 187, 255-268Ni, nickel, Nickel sulfide, NiS2, hydrophilic, hydrophobic, hydrophilicity, hydrophobocity, H2S, hydrogen sulfide, selective oxidation, stability
2001High-Yield Butane to Maleic Anhydride Direct Oxidation on Vanadyl Pyrophosphate Supported on Heat-Conductive Materials: β-SiC, Si3N4, and BNMarc J. Ledoux, Claude Crouzet, Cuong Pham-Huu, Vincent Turines, Kostantinos Kourtakis, Patrick L. Mills, Jan J. Lerou10.1006/jcat.2001.3344Studies in Surface Science and Catalysis, 1999, 126, 163-170butane, selective oxidation, maleic acid, VPO, vanadyl pyrophosphate, heat transfer, thermal conductivity, stability
2001Continuous process for selective oxidation of H2S over SiC-supported iron catalysts into elemental sulfur above its dewpointNicolas Keller, Cuong Pham-Huu, Marc J. Ledoux10.1016/S0926-860X(01)00601-9Catalysis Today, 1999, 53, 535-542H2S, hydrogen sulfide, selective oxidation, Fe, Fe2O3, iron, iron oxide, stability
2000Silicon carbide supported NiS2 catalyst for the selective oxidation of H2S in Claus tail-gasM.J. Ledoux, C. Pham-Huu, N. Keller, J.-B. Nougayrede, S. Savinponcet and J. Bousquet10.1016/S0920-5861(00)00365-5Applied Catalysis A: General, 1999, 185, 311-322H2S, hydrogen sulfide, selective oxidation, Ni, NiS2, nickel sulfide
2000Selective oxidation of H2S in Claus tail-gas over SiC supported NiS2 catalystMarc J. Ledoux, Cuong Pham-Huu, Nicolas Keller, Jean-B. Nougayrède, Sabine Savin-Poncet, Jacques Bousquet10.1016/S0920-5861(00)00365-5Applied Catalysis A: General, 1999, 181, 157-170Ni, nickel, Nickel sulfide, NiS2, hydrophilic, hydrophobic, hydrophobicity, hydrophilicity,H2S, hydrogen sulfide, oxisulfide, selective oxidation, stability
1999Characterization of the deactivation of MoO3-carbon-modified supported on SiC for n-butane dehydrogenation reactionBaudouin Heinrich, M. Elina Harlin, Cuong Pham-Huu, A. Outi, I. Krause, Marc J. Ledoux10.1016/S0167-2991(99)80463-7Applied Catalysis A: General, 1999, 180, 385-397n-butane, dehydrogenation, MoO3, molybdenum oxycarbide, deactivation, n-butane, dehydrogenation
1999Direct oxidation of H2S into S. New catalysts and processes based on SiC supportNicolas Keller, Cuong Pham-Huu, Claude Crouzet, Marc J. Ledoux, Sabine Savin-Poncet, Jean-B. Nougayrede, Jacques Bousquet10.1016/S0920-5861(99)00141-8Applied Catalysis A: General, 1997, 167, 321-330Ni, nickel, Nickel sulfide, NiS2, Fe, Fe2O3, iron, iron oxide, H2S, hydrogen sulfide, selective oxidation, stability
1999Part II. Dehydrogenation of n-butane over carbon modified MoO3 supported on SiCM. E. Harlin, A. O. I. Krause, B. Heinrich, C. Pham-Huu, M. J. Ledoux10.1016/S0926-860X(99)00190-8Journal De Physique IV France, 1997, 7, C1-677-C1-678dehydrogenation, n-butane, butane, MoOxCy, Mo, molybdenum oxycarbide, molybdenum oxide
1999Part I. n-Butane dehydrogenation on unsupported carbon modified MoO3 (MoOxCy): effect of steam on the catalyst stabilityMarc J. Ledoux, Frederic Meunier, Baudouin Heinrich, Cuong Pham-Huu, M. Elina Harlin, A. Outi I. Krause10.1016/S0926-860X(98)00417-7Catalysis Today, 1997, 35, 51-57dehydrogenation, isomerisation, n-butane, butane, MoOxCy, Mo, molybdenum oxicarbide, molybdenum oxide, MoO3, regeneration
1999High surface area silicon carbide doped with zirconium for use as catalyst support. Preparation, characterization and catalytic applicationCuong Pham-Huu, Christophe Bouchy, Thierry Dintzer, Gabrielle Ehret, Claude Estournes, Marc J. Ledoux10.1016/S0926-860X(98)00371-8Applied Catalysis A: General, 1997, 156, 131-149Zr, zirconium, dopant, high surface area, isomerisation, n-heptane, heptane, Mo, MoOxCy, mobybdenum oxycarbide, ZrO2, zirconia
1997Effect of the total activation pressure on the structural and catalytic performance of the SiC supported MoO3-carbon-modified catalyst for the n-heptane isomerizationPascal Del Gallo, Coung Pham-Huu, Christophe Bouchy, Claude Estournes, Marc J. Ledoux10.1016/S0926-860X(97)00004-5Current Opinion in Solid State and Materials Science, 1996, 1, 96-100n-heptane, isomerization, MoO3, Mo2C, carbide, molybdenum oxycarbide
1996Catalysis with carbidesMarc J Ledoux, Cuong Pham-Huu, Russ R Chianelli10.1016/S1359-0286(96)80016-7Applied Catalysis A: General, 1995, 132, 77-96transition metal carbides, three-way exhaust, automotive exhaust, TWC, selective hydrogenation, isomerization, Mo, molybdenum, oxycarbide, stability
1995n-Hexane and n-heptane isomerization at atmospheric and medium pressure on MoO3-carbon-modified supported on SiC and γ-Al2O3Cuong Pham-Huu, Pascal Del Gallo, Eric Peschiera, Marc J. Ledoux10.1016/0926-860X(95)00151-4Catalysis Today, 1995, 23, 283-298isomerization, n-heptane, n-hexane, MoO3, molybdenum, oxycarbide, stability
1995A sub-nanometer structural study of Pt-Rh catalysts supported on Ce doped SiCM. Benaissa, C. Pham-Huu, J. Werckmann, C. Crouzet, M.J. Ledoux10.1016/0920-5861(94)00168-2Applied Catalysis B: Environmental, 1994, 4, 45-63Ce, cerium, dopant, Pt, Rh, platine, rhodium, TEM
1994Synthesis and characterization of platinum-rhodium supported on SiC and SiC doped with cerium: Catalytic activity for the automobile exhaust reactionsPham-Huu Cuong, Sophie Marin, Marc J. Ledoux, Michel Weibel, Gabrielle Ehret, Mohamed Benaissa, Eric Peschiera, Jean Guille10.1016/0926-3373(94)00011-5Catalysis Today, 1992, 15, 263-284dopant, Ce, cerium, Pt, platinum, Rh, rhodium, automotive exhaust, stability
1992High specific surface area carbides of silicon and transition metals for catalysisM.J. Ledoux, C. Pham-Huu and with the collaboration of: J. Guille H. Dunlop, S. Hantzer, S. Marin, M. Weibel10.1016/0920-5861(92)80179-QJournal of Catalysis, 1988, 114, 176-185dopant, U, uranium, Ce, cerium, synthesis, preparation, carbides, transition metals, molybdenum carbide, Mo2C, tungsten carbide, WC, HDS, CoMo, hydrodesulfurization, thiophene, three-way exhaust catalysis, automotive exhaust, Pt, platinum, Rh, Rhodium, isomerisation, n-hexane, selective hehydrogenation, cyclohexane
1988New synthesis and uses of high-specific-surface SiC as a catalytic support that is chemically inert and has high thermal resistanceMarc J. Ledoux, Sylvain Hantzer, Cuong Pham Huu, Jean Guille, Marie-Pierre Desaneaux10.1016/0021-9517(88)90019-XApplied Catalysis, 1986, 20, 91-107synthesis, preparation, high surface area, dopant, uranium, HDS, hydrodesulfurization, CoMo