作者: Giuseppe Barbieri , Giuseppe Marigliano , Giovanni Perri , Enrico Drioli
DOI: 10.1021/IE0006211
关键词: Exothermic reaction 、 Thermodynamic equilibrium 、 Steam reforming 、 Isothermal process 、 Catalytic reforming 、 Thermodynamics 、 Reaction rate 、 Methane 、 Chemistry 、 Membrane reactor
摘要: An analysis of the conversion−temperature diagram for methane steam reforming is presented. A mathematical model a membrane reactor (MR) containing Pd-based with ideal behavior was developed to calculate temperature and species profiles. The comparison annular tubular configurations showed different MR performance because thermal effects. equilibrium system calculated, starting from method “reactors in series”. curve calculated as function sweep factor (I), defined ratio gas feed flow rates. existence region I delimited by adiabatic, isothermal, curves. Once I, molar ratio, oven were defined, reaction paths all MRs fell within region. This observed various values rates, thicknesses, overall heat transfer coefficients, geomet...