Theoretical analysis of the effect of catalyst mass distribution and operation parameters on the performance of a Pd-based membrane reactor for water–gas shift reaction

Sweep gas flow effect on membrane reactor performance for hydrogen production from high-temperature water-gas shift reaction

“…In Table 1, catalyst bed properties and reaction kinetic parameters are taken from the study of Adams and Barton [38]. The reaction side operating conditions and membrane properties are based on the studies of Augustine et al [12], Chiappetta et al [34], and our previous study [30]. As shown in our previous study [30], the numerical model was verified with the experimental data provided by Augustine et al [12].…”

“…1(b). The membrane tube has a length of 150 mm and radius (denoted as R R ) of 5 mm taken from the study of Chiappetta et al [34]. All other dimensions are specified to complete the reactor design.…”

Modeling and simulation of H2S effect in high-temperature water–gas shift reaction using coal-derived syngas

“…The length of the reactor is chosen as 150 mm [34]. The catalyst bed properties are taken from the study of Adams and Barton [35].…”

CFD Simulation of Water Gas Shift Membrane Reactor--Pressure Effects on the Performance of the Reactor

“…They have suggested using the catalyst in the shell side for efficient heat transfer and better membrane utilization. Chiappetta et al (2008) using a 2D model found that the use of isothermal conditions in the model tends to over predict the membrane reactor performance. Adrover et al (2009) have developed a 1D pseudo homogeneous model and analyzed the effect of pressure, temperature and flow configuration on water gas shift membrane reactor.…”