Development of a Catalytic Fuel Processor for a 10 kW Combined Heat and Power System: Experimental and Modeling Analysis of the Steam Reforming Unit

被引:4
作者
Beretta, Alessandra [1 ]
Groppi, Gianpiero [1 ]
Ribani, Chiara [1 ]
Fares, Giuseppe [2 ]
Tregambe, Carlo [2 ]
机构
[1] Politecn Milan, Dipartimento Energia, Lab Catalysis & Catalyt Proc, Via Masa 33, I-20156 Milan, Italy
[2] ICI Caldaie SpA, Via G Pascoli 38, I-37059 Verona, Italy
关键词
steam reforming; CHP system; small scale H-2 production; reactor modelling;
D O I
10.3390/chemengineering2010005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, we address the development of a combined heat and power unit for residential applications, fed by natural gas, air and H2O; focus is on the design of the first catalytic stage of the fuel processor, that is the steam reforming unit. A commercial catalyst was tested at the laboratory scale, under kinetically controlled conditions in order to derive information on the reaction kinetics and support the basic engineering of the full scale reactor. Analogous tests after long term steam reforming ageing were then performed to quantify the evolution of the catalyst activity under real operating conditions and estimate a lumped deactivation factor. A modelling analysis was performed to predict the expected performance of the fuel processor at varying input parameters and catalyst activity profiles. It was verified that at a space velocity below 5000 Nl/kg(cat)/h, the reactor output is fully controlled by the thermodynamics at 650 degrees C, which guarantees the best operability and efficiency of the whole fuel processor.
引用
收藏
页码:1 / 19
页数:19
相关论文
共 42 条
[1]   Transition to renewable energy systems with hydrogen as an energy carrier [J].
Barbir, Frano .
ENERGY, 2009, 34 (03) :308-312
[2]  
BARTHOLOMEW CH, 1994, STUD SURF SCI CATAL, V88, P1
[3]   Development of a micro-cogeneration laboratory and testing of a natural gas CHP unit based on PEM fuel cells [J].
Campanari, S. ;
Valenti, G. ;
Macchi, E. ;
Lozza, G. ;
Ravida, N. .
APPLIED THERMAL ENGINEERING, 2014, 71 (02) :714-720
[4]   Catalytic partial oxidation of n-octane and isooctane: Experimental and modeling results [J].
Carrera, Andrea ;
Pelucchi, Matteo ;
Stagni, Alessandro ;
Beretta, Alessandra ;
Groppi, Gianpiero .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2017, 42 (39) :24675-24688
[5]   Integration of Methane Steam Reforming and Water Gas Shift Reaction in a Pd/Au/Pd-Based Catalytic Membrane Reactor for Process Intensification [J].
Castro-Dominguez, Bernardo ;
Mardilovich, Ivan P. ;
Ma, Liang-Chih ;
Ma, Rui ;
Dixon, Anthony G. ;
Kazantzis, Nikolaos K. ;
Ma, Yi Hua .
MEMBRANES, 2016, 6 (03)
[6]   A review on development of industrial processes and emerging techniques for production of hydrogen from renewable and sustainable sources [J].
Chaubey, Rashmi ;
Sahu, Satanand ;
James, Olusola O. ;
Maity, Sudip .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 23 :443-462
[7]   Surface Reaction Kinetics of Steam- and CO2-Reforming as Well as Oxidation of Methane over Nickel-Based Catalysts [J].
Delgado, Karla Herrera ;
Maier, Lubow ;
Tischer, Steffen ;
Zellner, Alexander ;
Stotz, Henning ;
Deutschmann, Olaf .
CATALYSTS, 2015, 5 (02) :871-904
[8]   Investigating the Plasma-Assisted and Thermal Catalytic Dry Methane Reforming for Syngas Production: Process Design, Simulation and Evaluation [J].
Delikonstantis, Evangelos ;
Scapinello, Marco ;
Stefanidis, Georgios D. .
ENERGIES, 2017, 10 (09)
[9]   Effect of pressure in the autothermal catalytic partial oxidation of CH4 and C3H8: Spatially resolved temperature and composition profiles [J].
Donazzi, A. ;
Livio, D. ;
Diehm, C. ;
Beretta, A. ;
Groppi, G. ;
Forzatti, P. .
APPLIED CATALYSIS A-GENERAL, 2014, 469 :52-64
[10]   Catalytic partial oxidation of methane over a 4% Rh/α-Al2O3 catalyst Part I:: Kinetic study in annular reactor [J].
Donazzi, Alessandro ;
Beretta, Alessandra ;
Groppi, Gianpiero ;
Forzatti, Pio .
JOURNAL OF CATALYSIS, 2008, 255 (02) :241-258