H2 production by methane steam reforming over Rh/Al2O3 catalyst packed in Cu foams: A strategy for the kinetic investigation in concentrated conditions

被引:30
作者
Ambrosetti, Matteo [1 ]
Bonincontro, Danilo [1 ]
Balzarotti, Riccardo [1 ]
Beretta, Alessandra [1 ]
Groppi, Gianpiero [1 ]
Tronconi, Enrico [1 ]
机构
[1] Politecn Milan, Dipartimento Energia, Via Lambruschini 4, I-20156 Milan, Italy
基金
欧洲研究理事会;
关键词
Methane steam reforming kinetics; Hydrogen; Rhodium catalyst; Process intensification; Open-cell foams; WATER-GAS SHIFT; PARTIAL OXIDATION; THERMAL-CONDUCTIVITY; CO2;
D O I
10.1016/j.cattod.2021.06.003
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The concept of Rh/Al2O3 catalyst pellets packed in highly conductive copper foams has been successfully tested in methane steam reforming showing the beneficial effects of thermal conductivity on the obtainment of gradient-less radial temperature profiles. In this work, the same concept is proposed as a strategy for the lab-scale kinetic investigation under concentrated conditions at ambient pressure; thanks to the homogeneous heating of the catalyst mass across the reactor section and the measurement of axial temperature profiles, well-controlled temperature conditions are obtained, and the experimental investigation can be extended to usually unfeasible conditions of high reactant concentrations, overcoming the typical challenges for the kinetic study. Here, steam reforming experiments were performed with CH4 and H2O feed molar fractions in the ranges of 10-20 % and 40-90 %, respectively. The co-feed of CO and H-2 was also investigated. A kinetic scheme was developed that substantially confirmed the main results of previous kinetic investigations in annular micro-reactor, performed under diluted conditions; in particular, the first order dependence of the rate of steam reforming on methane partial pressure, the independence from H2O partial pressure, and the important inhibiting effect of CO were confirmed. The independence of the reaction rate from the H-2 co-feed was here demonstrated for the first time. The new experimental campaign allowed to identify more clearly the kinetic dependencies of the water gas shift reaction, positively influenced by H2O partial pressure but scarcely affected by CO partial pressure, which could be also explained based on the inhibiting effect of surface CO coverage. Parameter estimates were obtained by model fit over a wide temperature range (400-850 degrees C), conveying robustness to the proposed kinetic scheme for future reactor design applications.
引用
收藏
页码:107 / 118
页数:12
相关论文
共 39 条
  • [1] Development of a heat transport model for open-cell metal foams with high cell densities
    Aghaei, Pedram
    Visconti, Carlo Giorgio
    Groppi, Gianpiero
    Tronconi, Enrico
    [J]. CHEMICAL ENGINEERING JOURNAL, 2017, 321 : 432 - 446
  • [2] Packed foams for the intensification of catalytic processes: assessment of packing efficiency and pressure drop using a combined experimental and numerical approach
    Ambrosetti, Matteo
    Bracconi, Mauro
    Maestri, Matteo
    Groppi, Gianpiero
    Tronconi, Enrico
    [J]. CHEMICAL ENGINEERING JOURNAL, 2020, 382
  • [3] [Anonymous], 2019, HYDROGEN ROADMAP EUR, DOI [10.2843/249013, DOI 10.2843/249013]
  • [4] [Anonymous], 2011, Introduction to Optimum Design, DOI [10.1016/C2013-0-15344-5, DOI 10.1016/C2013-0-15344-5]
  • [5] Methane steam reforming in a microchannel reactor for GTL intensification: A computational fluid dynamics simulation study
    Arzamendi, G.
    Dieguez, P. M.
    Montes, M.
    Odriozola, J. A.
    Sousa-Aguiar, E. Falabella
    Gandia, L. M.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2009, 154 (1-3) : 168 - 173
  • [6] Experimental Insights into the Coupling of Methane Combustion and Steam Reforming in a Catalytic Plate Reactor in Transient Mode
    Ashraf, M. Arsalan
    Tacchino, Stefano
    Peela, Nageswara Rao
    Ercolino, Giuliana
    Gill, Kirandeep K.
    Vlachos, Dionisios G.
    Specchia, Stefania
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2021, 60 (01) : 196 - 209
  • [7] Investigation of packed conductive foams as a novel reactor configuration for methane steam reforming
    Balzarotti, Riccardo
    Ambrosetti, Matteo
    Beretta, Alessandra
    Groppi, Gianpiero
    Tronconi, Enrico
    [J]. CHEMICAL ENGINEERING JOURNAL, 2020, 391
  • [8] A comparison between washcoated and packed copper foams for the intensification of methane steam reforming
    Balzarotti, Riccardo
    Beretta, Alessandra
    Groppi, Gianpiero
    Tronconi, Enrico
    [J]. REACTION CHEMISTRY & ENGINEERING, 2019, 4 (08) : 1387 - 1392
  • [9] Testing in annular micro-reactor and characterization of supported Rh nanoparticles for the catalytic partial oxidation of methane: Effect of the preparation procedure
    Beretta, Alessandra
    Donazzi, Alessandro
    Groppi, Gianpiero
    Forzattl, Pio
    Dal Santo, Vladirniro
    Sordelli, Laura
    De Grandi, Valentina
    Psaro, Rinaldo
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2008, 83 (1-2) : 96 - 109
  • [10] Development of a Catalytic Fuel Processor for a 10 kW Combined Heat and Power System: Experimental and Modeling Analysis of the Steam Reforming Unit
    Beretta, Alessandra
    Groppi, Gianpiero
    Ribani, Chiara
    Fares, Giuseppe
    Tregambe, Carlo
    [J]. CHEMENGINEERING, 2018, 2 (01) : 1 - 19