Kinetic Evaluation of Carbon Formation in a Membrane Reactor for Methane Reforming

M. N. PEDERNERA; J. PIÑA; D.O. BORIO

CHEMICAL ENGINEERING JOURNAL

Elsevier

Año: 2007 vol. 134 p. 138 - 144

1385-8947

In the presentwork, the effect of hydrogen removal on carbon formation in a membrane reactor (with nickel supported catalyst) for steam andCO2 methane reforming is analyzed. The steady-state operation of the membrane reactor is described by means of a one-dimensional, heterogeneous, non-isothermal mathematical model. The carbon formation is kinetically evaluated through expressions reported in the literature. Higher CO2 contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. methane reforming is analyzed. The steady-state operation of the membrane reactor is described by means of a one-dimensional, heterogeneous, non-isothermal mathematical model. The carbon formation is kinetically evaluated through expressions reported in the literature. Higher CO2 contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. methane reforming is analyzed. The steady-state operation of the membrane reactor is described by means of a one-dimensional, heterogeneous, non-isothermal mathematical model. The carbon formation is kinetically evaluated through expressions reported in the literature. Higher CO2 contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle. contents in the feed stream or operating temperatures increase the risk of carbon formation in both, the membrane and conventional fixed bed reactors. Moreover, for a given feed composition and tube-wall temperature profile, the tendency to carbon deposition is promoted by hydrogen removal and increases as the percentage of hydrogen removed is augmented (for example, by a diminution of the Pd membrane thickness). The proposed model is a useful tool to predict the position where carbon formation is expected in the conventional and membrane reactors for methane reforming, not only along the catalyst tube but also within the Ni particle.