A simulation of a membrane reactor for the water gas shift reaction is carried out by means of a 1D pseudo-homogeneous nonisothermal mathematical model. The composite membrane consists of a dense layer of Pd (selective to H2) supported over a porous ceramic layer. The effect of temperature, overall heat-transfer coefficient, and mode of operation on the membrane reactor performance and stability are analyzed, and the results obtained are compared with those corresponding to a reactor with no hydrogen permeation. © 2009 American Institute of Chemical Engineers.Fil: Adrover, María Esperanza. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Un...
AbstractA dynamic model of a palladium membrane reactor for the Water Gas Shift (WGS) reaction has b...
The potential of using various types and configurations of membranes in reactors attracts already a ...
A theoretical study of a multitubular membrane reactor for the autothermal reforming of methane over...
A simulation study of a membrane reactor for the water-gas shift reaction is presented. A pseudohomo...
Fil: Adrover, María Esperanza. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Ci...
Water gas shift (WGS) is a thermodynamically limited reaction which has to operate at low temperatur...
A membrane reactor is a promising device to produce pure hydrogen and enrich CO2 from syngas. A simu...
Membrane reactors are attracting increasing interest because of the opportunity they represent in in...
The water-gas shift reaction is an exothermic and reversible catalytic process that converts carbon ...
Nowadays, most reactions in chemical and petrochemical industries are catalytic due to their enhanc...
Inorganic membranes for gas separation and purification have attracted great research interest. One ...
This work is focused on the integration of palladium membranes, permeable to hydrogen, in tubular c...
The water gas shift (WGS) reaction of a syngas mixture has been carried out in a tubular palladium m...
The concept of a CO 2 selective water gas shift (WGS) membrane reactor has been modeled and simulate...
Graduation date: 1992The purpose of this research is to study the\ud feasibility of combining reacti...
AbstractA dynamic model of a palladium membrane reactor for the Water Gas Shift (WGS) reaction has b...
The potential of using various types and configurations of membranes in reactors attracts already a ...
A theoretical study of a multitubular membrane reactor for the autothermal reforming of methane over...
A simulation study of a membrane reactor for the water-gas shift reaction is presented. A pseudohomo...
Fil: Adrover, María Esperanza. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Ci...
Water gas shift (WGS) is a thermodynamically limited reaction which has to operate at low temperatur...
A membrane reactor is a promising device to produce pure hydrogen and enrich CO2 from syngas. A simu...
Membrane reactors are attracting increasing interest because of the opportunity they represent in in...
The water-gas shift reaction is an exothermic and reversible catalytic process that converts carbon ...
Nowadays, most reactions in chemical and petrochemical industries are catalytic due to their enhanc...
Inorganic membranes for gas separation and purification have attracted great research interest. One ...
This work is focused on the integration of palladium membranes, permeable to hydrogen, in tubular c...
The water gas shift (WGS) reaction of a syngas mixture has been carried out in a tubular palladium m...
The concept of a CO 2 selective water gas shift (WGS) membrane reactor has been modeled and simulate...
Graduation date: 1992The purpose of this research is to study the\ud feasibility of combining reacti...
AbstractA dynamic model of a palladium membrane reactor for the Water Gas Shift (WGS) reaction has b...
The potential of using various types and configurations of membranes in reactors attracts already a ...
A theoretical study of a multitubular membrane reactor for the autothermal reforming of methane over...